Sygouni Varvara, Pantziaros Alexis G, Iakovides Iakovos C, Sfetsa Evangelia, Bogdou Polychronia I, Christoforou Emilia A, Paraskeva Christakis A
Department of Chemical Engineering, University of Patras, GR-26504 Patras, Greece.
Foundation for Research and Technology Hellas, Institute of Chemical Engineering Science, Stadiou Str., Platani, GR-26504 Patras, Greece.
Membranes (Basel). 2019 Feb 5;9(2):27. doi: 10.3390/membranes9020027.
The semi-solid wastes (pomace or alperujo) produced in the two-phase olive oil extraction process contains extremely high organic load and phenolic substances. Efficient treatment of such kinds of wastes using membrane filtration, should be sought to reduce the hazardous effects to the environment. On the other hand, phenolic compounds can be isolated and purified up to a level of commercial exploitation using the membrane technology. Firstly, the extraction process with mixtures of water and ethanol was optimized by testing extraction parameters (e.g., solvent's mixture, duration, and temperature) at laboratory scale. Next, extraction was conducted using larger volumes and the treatment was continued in a pilot membrane filtration system, consisted of ultrafiltration (UF), nanofiltration (NF) and reverse osmosis (RO) membranes. The extracted solution from the olive oil pomace was fed to the pilot membrane filtration system, where all fat, lipids, and solids were removed while the phenolic compounds were concentrated in the retentate streams of NF and/or RO. Total phenolic content (TPC) at the RO's concentrate stream was 225 mg/L and at the final effluent was lower than 10 mg/lt. The chemical oxygen demand (COD) value at the final effluent was much lower (~280 mg/L) than in the feed stream (>32,000 mg/L).
两相橄榄油提取过程中产生的半固体废弃物(果渣或alperujo)含有极高的有机负荷和酚类物质。应寻求采用膜过滤技术对这类废弃物进行有效处理,以减少其对环境的有害影响。另一方面,可以使用膜技术分离和纯化酚类化合物,直至达到商业开发的水平。首先,通过在实验室规模测试提取参数(如溶剂混合物、持续时间和温度),对水和乙醇混合物的提取过程进行了优化。接下来,使用更大的体积进行提取,并在由超滤(UF)、纳滤(NF)和反渗透(RO)膜组成的中试膜过滤系统中继续进行处理。将橄榄油果渣的提取液送入中试膜过滤系统,在该系统中,所有的脂肪、脂质和固体都被去除,而酚类化合物则浓缩在纳滤和/或反渗透的截留液流中。反渗透浓缩液流中的总酚含量(TPC)为225 mg/L,最终出水的总酚含量低于10 mg/L。最终出水的化学需氧量(COD)值(约280 mg/L)远低于进料流中的值(>32,000 mg/L)。