Department of Chemical Engineering - Lund University, P,O, Box 124, S-22100 Lund, Sweden.
Biotechnol Biofuels. 2012 Apr 13;5:22. doi: 10.1186/1754-6834-5-22.
Bioethanol produced from the lignocellulosic fractions of sugar cane (bagasse and leaves), i.e. second generation (2G) bioethanol, has a promising market potential as an automotive fuel; however, the process is still under investigation on pilot/demonstration scale. From a process perspective, improvements in plant design can lower the production cost, providing better profitability and competitiveness if the conversion of the whole sugar cane is considered. Simulations have been performed with AspenPlus to investigate how process integration can affect the minimum ethanol selling price of this 2G process (MESP-2G), as well as improve the plant energy efficiency. This is achieved by integrating the well-established sucrose-to-bioethanol process with the enzymatic process for lignocellulosic materials. Bagasse and leaves were steam pretreated using H3PO4 as catalyst and separately hydrolysed and fermented.
The addition of a steam dryer, doubling of the enzyme dosage in enzymatic hydrolysis, including leaves as raw material in the 2G process, heat integration and the use of more energy-efficient equipment led to a 37 % reduction in MESP-2G compared to the Base case. Modelling showed that the MESP for 2G ethanol was 0.97 US$/L, while in the future it could be reduced to 0.78 US$/L. In this case the overall production cost of 1G + 2G ethanol would be about 0.40 US$/L with an output of 102 L/ton dry sugar cane including 50 % leaves. Sensitivity analysis of the future scenario showed that a 50 % decrease in the cost of enzymes, electricity or leaves would lower the MESP-2G by about 20%, 10% and 4.5%, respectively.
According to the simulations, the production of 2G bioethanol from sugar cane bagasse and leaves in Brazil is already competitive (without subsidies) with 1G starch-based bioethanol production in Europe. Moreover 2G bioethanol could be produced at a lower cost if subsidies were used to compensate for the opportunity cost from the sale of excess electricity and if the cost of enzymes continues to fall.
从甘蔗的木质纤维素部分(蔗渣和叶片)生产的生物乙醇,即第二代(2G)生物乙醇,作为汽车燃料具有广阔的市场潜力;然而,该工艺仍处于中试/示范规模的研究阶段。从工艺角度来看,改进工厂设计可以降低生产成本,如果考虑将整个甘蔗进行转化,那么将提高盈利能力和竞争力。本文使用 AspenPlus 进行了模拟,以研究过程集成如何影响这种 2G 工艺的最低乙醇销售价格(MESP-2G),并提高工厂的能源效率。这是通过将成熟的蔗糖转化为生物乙醇工艺与木质纤维素材料的酶解工艺集成来实现的。使用 H3PO4 作为催化剂对蔗渣和叶片进行蒸汽预处理,然后分别进行水解和发酵。
通过增加蒸汽干燥机、将酶剂量增加一倍以用于酶解、将叶片纳入 2G 工艺、热集成以及使用更节能的设备,与基准案例相比,MESP-2G 降低了 37%。模型表明,2G 乙醇的 MESP 为 0.97 美元/升,而未来可能降至 0.78 美元/升。在这种情况下,1G+2G 乙醇的总生产成本约为 0.40 美元/升,输出为 102 升/吨干甘蔗,包括 50%的叶片。对未来情景的敏感性分析表明,酶、电或叶片成本降低 50%,将使 MESP-2G 降低约 20%、10%和 4.5%。
根据模拟结果,巴西从蔗渣和叶片生产 2G 生物乙醇已经具有竞争力(无补贴),而欧洲基于淀粉的 1G 生物乙醇生产则不具有竞争力。此外,如果使用补贴来补偿销售多余电力的机会成本,并且如果酶的成本继续下降,那么 2G 生物乙醇的生产成本可能会更低。