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. 2021 May 28;11(6):407. doi: 10.3390/membranes11060407
APGA Annual production geranyl acetate (kg year−1)
cA Alcohol concentration (mol kg−1)
cB Methyl acetate concentration (mol kg−1)
CCAP Annualized capital investments (EUR year−1)
CGER Geraniol purchase cost (EUR year−1)
CL Labor cost (EUR year−1)
CMAC Methyl acetate purchase cost (EUR year−1)
CO&M Operational expenditures (EUR year−1)
cP Product ester concentration (mol kg−1)
cQ Methanol concentration (mol kg−1)
CCGA Conversion cost geranyl acetate (EUR kg−1)
E Ratio of catalyst mass to total substrate mass (g g−1)
GC-FID gas chromatography-flame ionization detector
GC-MS gas chromatography-mass spectrometry
GUI graphical user interface
ID Inner diameter (mm)
JB Methyl acetate flux (mol m−2 h−1)
JQ Methanol flux (mol m−2 h−1)
k1 Forward second-order reaction constant (kg mol−1 h−1)
k2 Backward second-order reaction constant (kg mol−1 h−1)
kcat Specific rate constant (kg mol−1 h−1)
KM,A Michaelis–Menten constant for alcohol (mol kg−1)
KM,B Michaelis–Menten constant for methyl acetate (mol kg−1)
L Length (mm)
LL Lower limit of the 95% confidence interval for the specific rate constant (kg mol−1 h−1)
m˙ molar flow rate (mol h−1)
MEHQ 4-methoxyphenol
MW Molecular weight (g mol−1)
OD Outer diameter (mm)
PCGA Production cost, geranyl acetate (EUR kg−1)
PVA polyvinyl alcohol
PTZ phenothiazine
r Productivity (g kg−1 h−1)
S Exchange surface of the pervaporation membrane (m2)
s.c. supercritical
UL Upper limit of the 95% confidence interval for the specific rate constant (kg mol−1 h−1)
xi mole fraction of component i in the feed
yi mole fraction of component i in the permeate