TY - JOUR
T1 - Separation of succinic acid from fermentation broth: dielectric exclusion, Donnan effect and diffusion as the most influential mass transfer mechanisms
AU - Mancini, Enrico
AU - Ramin, Pedram
AU - Styrbæck, Peter
AU - Bjergholt, Christian
AU - Soheil Mansouri, Seyed
AU - Gernaey, Krist V.
AU - Luo, Jianquan
AU - Pinelo, Manuel
PY - 2022
Y1 - 2022
N2 - Nanofiltration can be used to separate bio-succinic (SA) acid from other
organic acids in fermentation broth. However, commercial nanofiltration
membranes can be insufficiently selective since some produced organic
acids have similar molecular weights. SA production from biomass
fermentation entails separation of bio-succinic acid from the other
concomitantly produced organic acids such as acetate, formate, pyruvate
etc. In this study, five commercial nanofiltration membranes were tested
for succinic acid (SA) rejection and selectivity under dead-end and
crossflow modes of SA recovery from selected synthetic solutions and
real fermentation broth. SA rejections up to 94.1 ± 1.5 % and 95.5 ± 3.5
% were observed for the synthetic broth and the fermentation broth,
respectively. The SA fractions % obtained were nearly 70% and 60% for
synthetic and fermentation broth, respectively. The highest rejections
and SA fraction values were achieved with DK and NF270, which also
showed the highest permeate flux. Model evaluation using the
Donnan-steric pore model with dielectric exclusion (DSPM-DE) showed that
99% of the succinate rejection occurs at the membrane interface and not
inside the membrane. Based on the modelling, the most important
mechanism affecting separation was dielectric exclusion at both sides of
the membrane surfaces. Moreover, identified sensitive model parameters
pore dielectric constant , charge density and pore radius
were estimated through model fitting and were found to be highly
correlated, albeit with significant variations. Finally, for the first
time, a calibrated model with synthetic broth was successfully used to
predict organic acids rejection for a real fermentation broth (with 12%
and 3% prediction error for succinate rejection by NF270 and DK,
respectively). Such prediction was achieved only by measuring organic
acid concentrations in the fermentation broth and using the three
sensitive parameters. Furthermore, the potential contribution of
different transport mechanisms of SA was quantified for the first time.
AB - Nanofiltration can be used to separate bio-succinic (SA) acid from other
organic acids in fermentation broth. However, commercial nanofiltration
membranes can be insufficiently selective since some produced organic
acids have similar molecular weights. SA production from biomass
fermentation entails separation of bio-succinic acid from the other
concomitantly produced organic acids such as acetate, formate, pyruvate
etc. In this study, five commercial nanofiltration membranes were tested
for succinic acid (SA) rejection and selectivity under dead-end and
crossflow modes of SA recovery from selected synthetic solutions and
real fermentation broth. SA rejections up to 94.1 ± 1.5 % and 95.5 ± 3.5
% were observed for the synthetic broth and the fermentation broth,
respectively. The SA fractions % obtained were nearly 70% and 60% for
synthetic and fermentation broth, respectively. The highest rejections
and SA fraction values were achieved with DK and NF270, which also
showed the highest permeate flux. Model evaluation using the
Donnan-steric pore model with dielectric exclusion (DSPM-DE) showed that
99% of the succinate rejection occurs at the membrane interface and not
inside the membrane. Based on the modelling, the most important
mechanism affecting separation was dielectric exclusion at both sides of
the membrane surfaces. Moreover, identified sensitive model parameters
pore dielectric constant , charge density and pore radius
were estimated through model fitting and were found to be highly
correlated, albeit with significant variations. Finally, for the first
time, a calibrated model with synthetic broth was successfully used to
predict organic acids rejection for a real fermentation broth (with 12%
and 3% prediction error for succinate rejection by NF270 and DK,
respectively). Such prediction was achieved only by measuring organic
acid concentrations in the fermentation broth and using the three
sensitive parameters. Furthermore, the potential contribution of
different transport mechanisms of SA was quantified for the first time.
KW - Nanofiltration
KW - Organic acids
KW - DSPM-DE model
KW - Separation prediction
U2 - 10.1016/j.seppur.2021.119904
DO - 10.1016/j.seppur.2021.119904
M3 - Journal article
SN - 1383-5866
VL - 281
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 119904
ER -