A. Mati, M. Buffi, S. Dell’Orco, Giacomo Lombardi, Pilar Maria Ruiz Ramiro, S. Kersten, D. Chiaramonti
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引用次数: 3
Abstract
Fast pyrolysis of biomass is a well-known opportunity for sustainable alternative fuel production for transport and energy. However, bio-oils from biomass pyrolysis are viscous, acidic bio-crudes that need further steps of upgrading before being used either as fuels or chemicals. A process that is complementary to bio-oil hydrotreatment or co-processing consists of optimizing and tuning the upstream condensation steps of fast pyrolysis to separate and concentrate selected classes of compounds. This can be implemented by varying the condensation temperatures in a multi-step condensation unit. In this study, fractional condensation of fast pyrolysis vapors from pinewood has been applied to a bubbling fluidized bed reactor of 1 kg h−1 feed. The reactor was operated at 500 °C and connected to a downstream interchangeable condensation unit. Tests were performed using two different condensing layouts: (1) a series of two spray condensers and a tube-in-tube water-jacketed condenser, referred to as an intensive cooler; (2) an electrostatic precipitator and the intensive cooler. Using the first configuration, which is the focus of this study, high boiling point compounds—such as sugars and lignin-derived oligomers—were condensed at higher temperatures in the first stage (100–170 °C), while water-soluble lighter compounds and most of the water was condensed at lower temperatures and thus largely removed from the bio-oil. In the first two condensing stages, the bio-oil water content remained below 7% in mass (and therefore, the oil’s high calorific content reached 22 MJ kg−1) while achieving about 43% liquid yield, compared to 55% from the single-step condensation runs. Results were finally elaborated to perform a preliminary energy assessment of the whole system toward the potential upscaling of this fractional condensation approach. The proposed layout showed a significant potential for the upstream condensation step, simplifying the downstream upgrading stages for alternative fuel production from fast pyrolysis bio-oil.
快速热解生物质是一个众所周知的机会,可持续替代燃料生产的运输和能源。然而,来自生物质热解的生物油是粘性的、酸性的生物原油,在用作燃料或化学品之前需要进一步的升级步骤。作为生物油加氢处理或协同处理的补充,该过程包括优化和调整快速热解的上游冷凝步骤,以分离和浓缩选定的化合物类别。这可以通过改变多步骤冷凝装置中的冷凝温度来实现。在本研究中,松木快速热解蒸汽的分馏冷凝应用于1 kg h−1进料的鼓泡流化床反应器。反应器在500°C下运行,并连接到下游可互换冷凝装置。使用两种不同的冷凝布局进行了试验:(1)一系列两个喷雾冷凝器和一个管中管水套冷凝器,称为强化冷却器;(2)静电除尘器和强化冷却器。使用第一种结构,这是本研究的重点,高沸点化合物-如糖和木质素衍生的低聚物-在第一阶段(100-170°C)在较高温度下冷凝,而水溶性较轻的化合物和大部分水在较低温度下冷凝,从而从生物油中大部分去除。在前两个冷凝阶段,生物油的含水量保持在7%以下(因此,油的高热量含量达到22 MJ kg−1),同时获得约43%的产液率,而单步冷凝的产液率为55%。最后详细阐述了整个系统的初步能量评估,以实现这种分级冷凝方法的潜在升级。该布局显示了上游冷凝步骤的巨大潜力,简化了从快速热解生物油生产替代燃料的下游升级阶段。
期刊介绍:
Applied Sciences (ISSN 2076-3417) provides an advanced forum on all aspects of applied natural sciences. It publishes reviews, research papers and communications. Our aim is to encourage scientists to publish their experimental and theoretical results in as much detail as possible. There is no restriction on the length of the papers. The full experimental details must be provided so that the results can be reproduced. Electronic files and software regarding the full details of the calculation or experimental procedure, if unable to be published in a normal way, can be deposited as supplementary electronic material.