Sustainable ethanol production from lignocellulosic biomass – Application of exergy analysis
Introduction
The fast development of the world’s bioethanol industry has contributed to the debate on “food versus fuel” and the industry’s environmental impact. One of the largest potential feedstock for ethanol is lignocellulosic biomass which does not compete with food crops, specifically agricultural residues (e.g., sugarcane bagasse, crop straws, and corn stover), herbaceous crops (e.g., alfalfa, switchgrass), forestry wastes, wood, wastepaper, and municipal waste. Other point to be considered in biofuels production is “energy consumption vs. energy content in produced ethanol.” The processing of a renewable energy source usually involves the consumption of non-renewable resources (NRR). When the exergy content of an NRR is altered through an irreversible process, the environment is also considered altered. Hence, much research [1], [2], [3] has been undertaken on the exergy accounting of NRR consumption in order to measure the environmental impact of many manufacturing processes. According to WORC [4], the biomass energy should be grown or produced in a sustainable way that provides net environmental benefits. Biomass energy crops should be grown and harvested in a way that embodies best stewardship practices to maintain or improve air, water and soil quality. Among the criteria for judging sustainable biomass energy production, can be remarked the Net energy balance, which mentions that more energy should be released through biomass energy use than consumed in producing it (over its lifecycle). This includes energy consumed from planting, cultivating, and fertilizer or pesticide application, harvesting and transporting to market. Consequently, the second-generation biofuels represents a great alternative to reach the sustainability of this industry. In this sense, the global energy consumption in ethanol production from lignocellulosic residues, like bagasse, is lower than that of non residual energy crops because the residual biomass from existing sugar industry is used. As such the energy consumption for all farming stages of sugarcane is assumed by the traditional sugar production chain.
In accordance with Dincer and Rosen [5], sustainable development requires sustainable energy resources and the efficient use of such residues. Measuring the renewability of an energy resource using traditional energy accounting methods is also questionable since these methods are based on the first law of thermodynamics, which includes the principle of energy conservation. Moreover, a meaningful energy-related yield calculation, which would indicate if there is some type of actual net gain or loss during the utilization of an energy resource, should take into account the differences in all forms of energy (including the chemical energy of all materials) and the second law of thermodynamics, which recognizes changes in energy quality or usefulness [6]. Exergy analysis is a thermodynamic analysis technique based on the second law of thermodynamics which provides an alternative and illuminating means of assessing and comparing processes and systems rationally and meaningfully. In particular, exergy analysis yields efficiencies which provide a true measure of how nearly actual performance approaches the ideal, and identifies more clearly than energy analysis the causes and locations of thermodynamic losses and the impact on the natural environment. Consequently, exergy analysis can assist in improving and optimizing designs [7]. Exergy analysis is linked to sustainability because to increase the sustainability of energy use, we must be concerned not only with loss of energy, but also loss of energy quality (or exergy) [5]. One principal advantage of exergy analysis over energy analysis is that the exergy content of a process flows a better valuation of the flow than the energy content, since the exergy indicates the fraction of energy that is likely useful and thus utilizable. Application of exergy analysis to a component, process or sector can lead to insights into how to improve the sustainability of the activities comprising the system by reducing exergy losses. Thus, to justify the production of second-generation biofuels it is necessary to confirm that the energy produced from the lignocellulosic biomass is greater than the energy consumed in the ethanol production through exergy analysis. The main objective of this paper is to apply exergy analysis concept for the evaluation of the transformation of lignocellulosic biomass to bioethanol and to approach the sustainability of second-generation biofuels production. In the first part of the paper, the different processes involved in ethanol production from lignocellulosic biomass and the exergy analysis concept are described. In the second part, several case studies about lignocellulosic biomass transformation were selected and simulated using the typical daily amount of residual biomass produced by the sugar industry (1200 tonnes). Finally, the exergy analysis methodology was applied to evaluate of sustainability development of second-generation ethanol production. This methodology requires an analysis of each stage of the production process and the global evaluation of several scenarios of production to verify the sustainable development of the biofuels industry using lignocellulosic biomass.
Section snippets
Production of second-generation ethanol
The ethanol production from lignocellulosic biomass includes five main steps: biomass pre-treatment, cellulose hydrolysis, hexoses fermentation, separation and effluent treatment. Furthermore, detoxification and fermentation of pentoses released during the pre-treatment step can be carried out [8]. The sequential configuration employed to obtain cellulosic ethanol implies that the solid fraction of pretreated lignocellulosic material undergoes hydrolysis (saccharification); this fraction
Exergy analysis – Formulations
Exergy is the maximum amount of useful work that can be extracted from a physical system by exchanging matter and energy with large reservoirs through complete reversible process (heat transfer process, mass transfer process, chemical reaction etc.) in a reference stated by Shukuya and Hammache [11]. The energy and exergy balances for a flow process in a system during a finite time interval may be written as:
Selection of process topologies
Many flowsheet configurations have been proposed for ethanol production from lignocellulosic biomass, which incorporated pre-treatment, hydrolysis and fermentation steps [26], [27]. Numerous pre-treatment methods or combinations of pre-treatment methods are thus available, all having their specific advantages and disadvantages. The choice for a pre-treatment technology heavily influences cost and performance in subsequent hydrolysis and fermentation. To evaluate the second-generation biofuels
Results and discussion
Using Eqs. (1), (2), (3), (4), (5), (6), (7), (8), (9), (10), (11), (12), (13), exergy was calculated for all material streams in the process. The reference temperature was 25 °C, the relative humidity of atmospheric air was 70% and the chemical exergy of ash was neglected. The specific chemical exergies of the different components are listed in Table 4, based on values reported by Szargut et al. [17] and the application of equation (10). The values in Table 4 can be used to evaluate the
Conclusions
In this study, three different topologies for second-generation ethanol production from sugarcane bagasse were simulated and analyzed. The results show highest exergy efficiency in case 1 (Steam Explosion Pre-treatment + SSF + Dehydration) reaching 79.58%. The Case 2 (Acid diluted Pre-treatment + SSF + Dehydration) was showing lowest exergy efficiency (73.98%). For all cases, improvements in pre-treatment and SSF stages and design of heat network for thermal integration of the process are
Acknowledgements
The authors acknowledge the support provided by the Colombian Institute for Development of Science and Technology “Francisco Jose de Caldas” (COLCIENCIAS), Contract No 336-2007 “Optimization of joint production (sugar-alcohol) and development of new bioethanol production process” and the Ibero-American Program on Science and Technology for Development (CYTED), Project 306RTO279 “New technologies for biofuels production” UNESCO code: 330303, 332205, 530603, 330999.
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