Abstract:BACKGROUND: Energy efficient alternatives to distillation for alcohol recovery from dilute solution are needed to improve biofuel sustainability. A process integrating steam stripping with a vapor compression step and a vapor permeation membrane separation step is proposed. The objective of this work is to estimate the energy and process costs required to make a fuel grade ethanol (0.5 wt% water) from 1 and 5 wt% ethanol aqueous streams using the proposed process.
“…However, there is a drastic increase in the distillation energy demand as the ethanol concentration in the fermentation broth from cellulosic sources is relatively low (30,(37)(38)(39).…”
“…However, there is a drastic increase in the distillation energy demand as the ethanol concentration in the fermentation broth from cellulosic sources is relatively low (30,(37)(38)(39).…”
“…One of these is that most strains are sensitive to high ethanol concentrations [4,25]. This could be overcome by the continuous removal of ethanol as it is being produced, facilitated by the high volatility of the product at higher temperatures [25,71], or by engineering a strain tolerant to higher ethanol concentrations. Another negative aspect is the low ethanol yields produced, due to the formation of by-products such as lactate and acetate [25,70].…”
“…The typical separation process involves distillation near to the azeotropic point, followed by zeolite 3A adsorption or a steam membrane process using organic or zeolite 4A membranes. [8][9][10] However, this process is generally operated under high temperature and consumes a lot of heat energy. Alternatively, pervaporation process is a very promising technology as it can be operated under moderate working conditions.…”
Ethanediamine-modified zeolitic imidazolate framework (ZIF)-8 particles ) is synthesized and incorporated in the poly(vinyl alcohol) (PVA) matrix to fabricate novel PVA/ZIF-8-NH 2 mixed matrix membranes (MMMs) for pervaporation dehydration of ethanol. The PVA/ZIF-8-NH 2 MMMs exhibit enhanced membrane homogeneity and separation performance because of the higher hydrophilicity and restricted agglomeration of the particles, as compared to corresponding MMMs loaded with unmodified particles. The effect of ZIF-8-NH 2 loading in the MMMs is studied and the MMM with a 7.5 wt % ZIF-8-NH 2 loading shows the best pervaporation performance for ethanol dehydration at 408C. Various characterization techniques (Fourier transform infrared, scanning electron microscope, contact angle, sorption test, etc.) are used to investigate the MMMs loaded with ZIF-8 and ZIF-8-NH 2 particles. The impact of operation conditions on pervaporation performance is also performed. The performance benchmarking shows that the MMMs have superior separation factors and comparable flux to most other PVA hybrid membranes.
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