Pau Casademont-Lanzat, B. García-Jarana, Xiaowei Chen, Carol Carreño, J. Sánchez-Oneto, J. R. Portela, E. M. Ossa
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引用次数: 5
摘要
这项工作研究了使用橄榄油厂废物(OMW)作为亚临界或超临界水来生产液化生物燃料和气化气体燃料。液体和固体垃圾的数量不断增加,正成为一个严重的环境问题。这种废水具有很强的生物降解能力,含有多种化合物,如多酚、多元油、有机酸等,在排放前需要进行净化处理以去除气味和污染物负荷。本研究在不同的间歇反应器中,在温度为200 - 530 ÂoC和压力为150 - 250 bar的亚临界和超临界水中研究了OMW流的液化和气化。本研究还测试了各种类型的均相催化剂(KOH 0.01 g/g干样)和非均相催化剂(tio2、v2o和Au-Pd 0.1-0.5 g/g干样)对超临界水气化(SCWG)的有效性,并研究了它们对生物质转化率的影响方式。它还涵盖了使用不同有机化合物浓度(23、35和80 g o2 /l的化学需氧量浓度(COD))和成分(固体和液体OMW的混合物)对能源生产结果的影响。在最佳条件下(330 ÂoC, 150 bar,初始浓度23 g o2 /l,反应时间30 min), OMW水热液化的油收率最高可达82%。同时,以Au-Pd为催化剂气化OMW超临界水,产率为88.6 mol H 2 /kg OMW干。
Energy Production by Hydrothermal Treatment of Liquid and Solid Waste from Industrial Olive Oil Production
This work studies the use of olive oil mill waste ( OMW ) treated as subcritical or supercritical water to produce both, a biofuel by liquefaction and a gas fuel by gasification. The increasing amount of OMW , both liquid and solid, is becoming a serious environmental problem. This wastewater is highly resistant to biodegradation and contains a wide variety of compounds such as polyphenols, polyoils, organic acids, etc, that require depuration treatments to remove the odour and pollutant load before being discharged. This work studies both, liquefaction and gasification of OMW streams in subcritical and supercritical water in different batch reactors at temperatures between 200 and 530 ÂoC and pressures between 150 and 250 bar. This study also tests the effectiveness of various types of homogeneous (KOH 0.01 g/g sample dry ) and heterogeneous catalysts (TiO 2 , V 2 O 5 and Au-Pd 0.1-0.5 g/g sample dry ) for supercritical water gasification (SCWG) and studied the way they affect biomass conversion yields. It also covers the effect that the use of different organic compound concentrations (23, 35, and 80 g O 2 /l of chemical oxygen demand concentration (COD)) and compositions (mixtures of solid and liquid OMW ) has on energy production results. A maximum of 82% oil yield was obtained from the hydrothermal liquefaction of OMW under optimum conditions (330 ÂoC, 150 bar, 23 g O 2 /l as initial concentration and 30 minutes reaction time). Meanwhile, a yield of 88.6 mol H 2 /kg OMW dry was obtained when Au-Pd was used as a catalyst for the gasification of OMW supercritical water.