Please use this identifier to cite or link to this item: https://hdl.handle.net/10356/161991
Title: Economic analysis of membrane-based separation of biocatalyst: mode of operation and stage configuration
Authors: Kapavarapu, MSR Sridhar
Ma, Yunqiao
Vasudevan, Suraj V.
Chew, Jia Wei
Keywords: Engineering::Chemical technology
Issue Date: 2022
Source: Kapavarapu, M. S., Ma, Y., Vasudevan, S. V. & Chew, J. W. (2022). Economic analysis of membrane-based separation of biocatalyst: mode of operation and stage configuration. Industrial & Engineering Chemistry Research, 61(19), 6682-6692. https://dx.doi.org/10.1021/acs.iecr.2c00598
Project: A20B3a0070 
A2083c0049 
2019-T1-002-065 
RG100/19 
MOE-MOET2EP10120-0001 
Journal: Industrial & Engineering Chemistry Research
Abstract: As the use of biocatalyst proliferates due to the need for chirally pure active pharmaceutical ingredients (API), the corresponding separation of biocatalyst and API is crucial. Although economic analyses of membrane-filtration applications exist, one dedicated to the ultrafiltration of biocatalysts remained amiss, which motivated the current study. The costs for different operating modes (i.e., constant-flux or constant-TMP) and stage configurations (i.e., single versus multiple stages), as well as the effects of feed flow rate, flux, transmembrane pressure (TMP), membrane area, recovery, and filtration rate, were evaluated. The results indicate that a capital expenditure of $1.35 million and an annual operating expenditure of $85.6 thousand are needed to install a new ultrafiltration unit for a yearly permeation of 0.64 billion liters. While capital cost depends heavily on membrane area, operating cost depends on TMP and fluid flow across the unit.
URI: https://hdl.handle.net/10356/161991
ISSN: 0888-5885
DOI: 10.1021/acs.iecr.2c00598
Rights: © 2022 American Chemical Society. All rights reserved.
Fulltext Permission: none
Fulltext Availability: No Fulltext
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