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Sustainable Use of Digestate from Biogas Plants: Separation of Raw Digestate and Liquid Fraction Processing
This review provides an overview of the various aspects involved in the digestate separation process with a focus on the best solution. The paper discusses the possibility of processing the liquid fraction using membrane separation processes and evaporation. Despite the identical goal of digestate separation, the solutions presented have many differences. These differences affect each process’s capital, operating costs, efficiency, and complexity. Among the selected solutions, the most popular technology for separating digestate is a screw press. Its advantage is the simplicity of its design compared to the centrifuges or filter presses used. In addition to the economic aspect, a definite advantage of mechanical separation is the possibility of using the liquid fraction to reduce the dry matter of the feedstock for biogas plants. Regardless of the chosen technology, striving for the closed-cycle operation of biogas plants and optimizing production processes is now becoming necessary. Proper management of the digestate is a crucial element of the operational efficiency of any biogas plant in case of the sustainable energy. The prepared article will fill some gaps in knowledge and indicate further directions of action. It is necessary to further develop research on methods of digestate separation.
Research on a New Method of Water Recovery from Biogas Plant Digestate
Digestate is a product with valuable fertilizing properties, remaining after the anaerobic fermentation process. An essential feature of the substance in question is its high water content of up to 97%. To improve the fertilizer value of the digestate, it is necessary to dehydrate it to produce a concentrated product. This paper determined the possibility of dewatering the digestate using an innovative reactor design. The study, conducted on a laboratory scale, used digestate from a Polish biogas plant. The dewatering technique described in the paper is based on the evaporation and condensation of water vapor on the inner surface of the reactor dome. The condensate accumulated on the leach trough and was directed to a storage tank. During the weeks of testing, 11.5 kg of condensate was separated from the initial weight of the digestate (32 kg), with a dry weight of 6.11%. The resulting condensate from dehydration had an average pH value of 9.0 and an average ammonium nitrogen content of 2.07 g∙kg−1. The economic calculations made in the paper allowed for estimating the expected savings associated with the management of digestate in Poland. The research showed the proposed technology’s high potential for dewatering digestate under laboratory conditions.