Pyrolysis behavior and economics analysis of the biomass pyrolytic polygeneration of forest farming waste
Graphical abstract
Introduction
Over the past few decades, the “Returning Farmland to Forest” program has played an important role in the increase in forest coverage in China, albeit at the expense of farmland. To improve the living standards of the consequently landless farmers, forest farming has been vigorously supported by the Chinese government (He and Sikor, 2015). Some of the crops widely grown in Chinese forest farming include the Chinese chestnut and Jatropha curcas, well known as a delicious nut and biodiesel precursor (Sun et al., 2017b), respectively. Generally, the seeds of these crops are harvested with their shells; once the product is separated, waste Chinese chestnut shell (CNS) and J. curcas shell (JCS) remain. Typical forest waste (branches, bark, sawdust, etc.) is regarded as an important biomass resource (Chen et al., 2018b). However, the utilization of this new forest farming waste has not been researched or regulated, leaving it to be directly burned, likely in the farmer’s residential area, contributing to air pollution. Hence, it will be beneficial to both farmers and the environment if these wastes were converted to bioenergy, biofuels, or biomaterials using modern biomass conversion technologies (Wang et al., 2017, Zhang et al., 2017).
The process of biomass conversion can be divided into biochemical and thermochemical methods (Zhang et al., 2018). The latter includes combustion, gasification, and pyrolysis. Biomass combustion for heat or electricity is a quick method, but further development of this method is restricted by downsides such as the production of polluting particulates, and the huge costs involved for feedstock collection and transportation (Wang et al., 2014). Gasification is another effective method of converting biomass waste to syngas (CH4, H2, CO, CO2, etc.). However, the poor lower heating value (LHV; 3–5 MJ/m3) and high tar content of syngas from biomass gasification remain to be solved.
Pyrolysis can convert biomass into products of three states (tri-state) by heating in an inert atmosphere. These tri-state products, i.e., biogas, solid char, and liquid bio-oil, all have relatively high value or potential as intermediary products (Chen et al., 2012, Collard and Blin, 2014, Ji et al., 2017, Yang et al., 2016). Recently, biomass pyrolytic polygeneration of these products has been investigated as a promising conversion technology. Chen et al. studied the process of cotton stalk pyrolysis at laboratory scale, and found that 550–750 °C was a suitable operating temperature range (Chen et al., 2012). Yang et al. found that a commercial biomass pyrolytic polygeneration factory using retort reactors had high performance in converting straw to high-value products (Yang et al., 2016). Gao et al. investigated the effect of temperature during the pyrolysis of rapeseed stalk on the characteristics of the tri-state products, along with an economic analysis (Gao et al., 2017). They found that 350 and 650 °C were the optimum operating temperatures for char sold as solid fuel and activated char, respectively. However, these studies mainly focused on the pyrolysis of stalks; shells, as an abundant forest farming waste, were ignored. In addition, shells have high bulk density (∼0.42 g/cm3 for CNS and ∼0.49 g/cm3 for JCS) compared to stalks (∼0.11 g/cm3 for rapeseed stalk), which is good for transportation and economics Furthermore, CNS and JCS are easy to collect, as they are harvested with the seed product, while the collection of stalks faces problems due to their scattered distribution. Thus, the high bulk density and low collection cost of shell forest farming waste makes it suitable for biomass pyrolytic polygeneration.
Herein, two typical forest farming wastes were converted using a pyrolytic polygeneration system. The products were characterized by various analyses to speculate on potential applications. Furthermore, an economic analysis was performed based on the use of a moving bed. These data were used to elucidate the optimum processing condition for biomass pyrolytic polygeneration when using shells waste as feedstock. It is expected that commercial-scale biomass pyrolytic polygeneration can be utilized for the effective conversion of the abundant shell waste in China.
Section snippets
Materials
JCS was collected from Kunming, Yunnan province, and CNS was collected from Xiaogan, Hubei province in China. Samples were stored in a well ventilated space. Before the experiment, the samples were crushed and sieved to obtain a powder with a particle size of <2 mm. Proximate analysis of the samples was carried out in a TGA-2000 analyzer (Las Navas, Spain), and ultimate analysis was carried out with a CHN/O elementary analyzer (vario MICRO cube, Elementar, Germany). The lower heating value
Product yield distributions and properties of the gas and liquid products
The yield distributions of the final products from the two shell samples pyrolyzed at various temperatures are shown in Fig. 1a and b. For CNS, the char yield decreased rapidly to 31% as the temperature rose from 250 to 450 °C, and then the decreased slowly to 25% as the temperature increased further to 950 °C. This suggested that the main decomposition of the solid phase took place between 250 and 450 °C. The bio-oil yield initially increased as the temperature increased, then reached a
Conclusions
Biomass pyrolytic polygeneration proved to be an effective method of converting shell waste into high value products. The properties of the products can be tuned simply by changing the operating temperature. Different char evolution tendencies were found for CNS and JCS, and economic analysis suggested that the optimum operating temperatures were 450 °C for CNS and 350 °C for JCS in a commercial biomass pyrolytic polygeneration system.
Acknowledgement
The authors wish to express their great appreciation for the financial support of the National Natural Science Foundation of China (51622604, 51406061) and the Fundamental Research Funds for the Central Universities, and for the technical support from the Analytical and Testing Center at Huazhong University of Science & Technology (http://atc.hust.edu.cn).
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