Energy Recovery from Garden and Park Waste by Hydrothermal Carbonization with Process Water Recycling

被引:4
|
作者
Ipiales, Ricardo Paul [1 ,2 ]
Pimentel-Betancurt, Diana [1 ,3 ]
Diaz, Elena [1 ]
de la Rubia, Angeles [1 ]
Rodriguez, Juan J. [1 ]
Mohedano, Angel F. [1 ]
机构
[1] Univ Autonoma Madrid, Chem Engn Dept, Madrid 28049, Spain
[2] Arquimea Agrotech, Madrid 28400, Spain
[3] Univ Nacl Rio Cuarto, Mol Biol Dept, FCEFQyN, RA-5800 Cordoba, Argentina
关键词
anaerobic digestion; garden and parkwaste; hydrochar; hydrothermal carbonization; processwater recycling; MUNICIPAL SOLID-WASTE; SURFACE-CHEMISTRY; ORGANIC FRACTION; LIQUID FRACTION; SWINE MANURE; BIOMASS; HYDROCHAR; RECIRCULATION; DIGESTION; PRODUCTS;
D O I
10.1021/acssuschemeng.3c08438
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
This study aims to obtain a carbonaceous material with suitable properties to be used as a solid biofuel by recycling process water from hydrothermal carbonization (HTC) of garden and park waste (GPW). The research is focused on maximizing mass yield and energy recovery as well as facilitating the treatment of the liquid fraction throughout reusing cycles of the liquid fraction. Process water recycling moderately improved the mass performance of the hydrochar, resulting in a higher energy recovery of almost 20 percentage points compared with that achieved (less than 79%) with conventional HTC (GPW + freshwater feed). An improvement in char fuel quality was observed, showing more suitable morphological, physical, and chemical characteristics, higher reactivity and combustion temperature, and lower probability of ash sintering. Successive process water reuse cycles allowed some increase in energy yield but, at the same time, degraded the quality of hydrochar as a biofuel. Process water composition showed an increase in chemical oxygen demand and total organic carbon, which almost doubled after three successive reuse cycles. The concentration of volatile fatty acids increased around 5-fold (up to 20 g L-1), with acetic acid accounting for 85% of the total. Subsequent anaerobic digestion of the process water removed up to 75% of the COD and yielded a biogas with high methane content (225-302 N mL CH4 g(-1) CODadded). Recycling of the process water significantly improved the total energy recovery (hydrochar + methane) to 90% after a single recycling, compared to 84% achieved with conventional HTC and subsequent anaerobic treatment of the resulting process water.
引用
收藏
页码:5229 / 5240
页数:12
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