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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Energetic comparison for leaching waste liquid from citric juice production using both reverse osmosis and multiple-effect evaporation
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Energetic comparison for leaching waste liquid from citric juice production using both reverse osmosis and multiple-effect evaporation

机译:利用反渗透和多效蒸发法从柠檬汁生产中浸出废液的能量比较

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In citric juice production a waste leaching liquid stream is obtained.This stream contains a high level of sucrose(about 10 deg Brix)which makes its pouring into the public sewer inconvenient and even illegal since it can become a great environmental problem.It is,therefore,necessary to find a valorization way for these pollutant streams.A sucrose concentration contained in the leaching stream is proposed in order to get citrus molasses and a water stream which could be reused in the citric juice process.To achieve these valorized streams,there are two main possibilities:the first one is the use of a membrane technology such as reverse osmosis(RO)as a preconcentration system until 25-30 deg Brix [ 1 ] with later evaporation to 65 deg Brix,whereas the second one is the use of a multiple-effect evaporation(MEE)system.The election of the concentration option,out of other factors,depends on the energy consumption that both alternatives have for the same concentration level.The aim of this work is firstly to get a model function describing the RO experimental process to design series-parallel systems.Secondly,to select a design among different systems considered.Energy consumption requirements by both RO and MEE were calculated and compared.In a design using 24 membrane elements,it was found that RO had a 7.7 times lower consumption than MEE.
机译:在柠檬汁生产中,获得了一种废物浸出液流,其中含有高水平的蔗糖(大约10度白利糖度),这使其倒入公共下水道不方便甚至是非法的,因为它可能会成为一个严重的环境问题。因此,有必要为这些污染物流寻找一种增值方法。提出了一种浸出流中所含的蔗糖浓度,以获得柑橘糖蜜和可在柠檬酸汁工艺中重复使用的水流。要实现这些增值流,需要主要有两种可能性:第一种是使用膜技术,例如反渗透(RO)作为预浓缩系统,直到25-30度白利糖度[1],然后蒸发到65度白利糖度,而第二种是使用选择多效蒸发(MEE)系统。出于其他因素的考虑,选择集中度方案取决于两个方案在相同集中度水平下的能耗。首先要获得描述反渗透实验过程的模型函数,以设计串联-并联系统。其次,在考虑的不同系统中选择一个设计。计算并比较反渗透和MEE的能耗要求。在使用24膜的设计中元素,发现RO的消耗量比MEE低7.7倍。

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