Department of Agricultural and Environmental Sciences (DISA), University of Udine, Italy.
Waste Manag. 2013 Jun;33(6):1339-44. doi: 10.1016/j.wasman.2013.02.023. Epub 2013 Apr 4.
Vacuum evaporation consists in the boiling of a liquid substrate at negative pressure, at a temperature lower than typical boiling temperature at atmospheric conditions. Condensed vapor represents the so called condensate, while the remaining substrate represents the concentrate. This technology is derived from other sectors and is mainly dedicated to the recovery of chemicals from industrial by-products, while it has not been widely implemented yet in the field of agricultural digestate treatment. The present paper relates on experimental tests performed in pilot-scale vacuum evaporation plants (0.100 and 0.025 m(3)), treating filtered digestate (liquid fraction of digestate filtered by a screw-press separator). Digestate was produced by a 1 MWe anaerobic digestion plant fed with swine manure, corn silage and other biomasses. Different system and process configurations were tested (single-stage and two-stage, with and without acidification) with the main objectives of assessing the technical feasibility and of optimizing process parameters for an eventual technology transfer to full scale systems. The inputs and outputs of the process were subject to characterization and mass and nutrients balances were determined. The vacuum evaporation process determined a relevant mass reduction of digestate. The single stage configuration determined the production of a concentrate, still in liquid phase, with a total solid (TS) mean concentration of 15.0%, representing, in terms of mass, 20.2% of the input; the remaining 79.8% was represented by condensate. The introduction of the second stage allowed to obtain a solid concentrate, characterized by a content of TS of 59.0% and representing 5.6% of initial mass. Nitrogen balance was influenced by digestate pH: in order to limit the stripping of ammonia and its transfer to condensate it was necessary to reduce the pH. At pH 5, 97.5% of total nitrogen remained in the concentrate. This product was characterized by very high concentrations of total Kjeldhal nitrogen (TKN), 55,000 mg/kg as average. Condensate, instead, represented 94.4% of input mass, containing 2.5% of TKN. This fraction could be discharged into surface water, after purification to meet the criteria imposed by Italian regulation. Most likely, condensate could be used as dilution water for digestion input, for cleaning floor and surfaces of animal housings or for crop irrigation. The research showed the great effectiveness of the vacuum evaporation process, especially in the two stage configuration with acidification. In fact, the concentration of nutrients in a small volume determines easier transportation and reduction of related management costs. In full scale plants energy consumption is estimated to be 5-8 kWh e/m(3) of digestate and 350 kWh t/m(3) of evaporated water.
真空蒸发是指在负压下将液体基质煮沸,温度低于常压下的典型沸点。冷凝蒸汽代表所谓的冷凝物,而剩余的基质代表浓缩物。这项技术源自其他领域,主要用于从工业副产品中回收化学品,而在农业消化物处理领域尚未得到广泛应用。本文介绍了在中试规模的真空蒸发装置(0.100 和 0.025m3)中进行的实验测试,该装置处理过滤后的消化物(螺旋压榨分离器过滤的消化物的液体部分)。消化物由一个 1MWe 的厌氧消化厂生产,使用猪粪、玉米青贮和其他生物质。测试了不同的系统和工艺配置(单级和两级,有和没有酸化),主要目的是评估技术可行性,并优化工艺参数,以便将来转移到全规模系统。过程的输入和输出都进行了特性描述,并确定了质量和养分平衡。真空蒸发过程使消化物的质量显著减少。单级配置可生产仍处于液相的浓缩物,总固体(TS)平均浓度为 15.0%,按质量计,占输入量的 20.2%;剩余的 79.8%由冷凝物组成。引入第二级可获得固体浓缩物,其总固体(TS)含量为 59.0%,占初始质量的 5.6%。氮平衡受消化物 pH 的影响:为了限制氨的汽提及其向冷凝物的转移,有必要降低 pH 值。在 pH 值为 5 时,总氮的 97.5%仍留在浓缩物中。该产品的总凯氏氮(TKN)浓度非常高,平均为 55000mg/kg。而冷凝物则占输入质量的 94.4%,含有 2.5%的 TKN。该馏分可排入地表水,经净化后达到意大利法规规定的标准。很可能,冷凝物可作为消化物输入的稀释水,用于清洁动物圈舍的地板和表面,或用于灌溉作物。研究表明,真空蒸发工艺非常有效,尤其是在酸化的两级配置中。事实上,浓缩物中养分的浓度较小,可更方便地运输,降低相关管理成本。在全规模工厂中,估计每立方米消化物消耗 5-8kWh 的电能,每立方米蒸发水消耗 350kWh 的电能。