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开发一种真空热汽提-酸吸收工艺,从厌氧消化器废水中回收氨。

Developing a vacuum thermal stripping - acid absorption process for ammonia recovery from anaerobic digester effluent.

机构信息

Department of Environmental Resources Engineering, College of Environmental Science and Forestry, State University of New York, 1 Forestry Dr., Syracuse, NY 13210, USA.

Department of Environmental Resources Engineering, College of Environmental Science and Forestry, State University of New York, 1 Forestry Dr., Syracuse, NY 13210, USA.

出版信息

Water Res. 2016 Dec 1;106:108-115. doi: 10.1016/j.watres.2016.09.054. Epub 2016 Sep 27.

Abstract

To prevent acetoclastic methanogens from ammonia inhibition in anaerobic digestion of protein-rich substrates, ammonia needs to be removed or recovered from digestate. This paper presents an innovative ammonia recovery process that couples vacuum thermal stripping with acid absorption. Ammonia is stripped out of digestate boiling at a temperature below the normal boiling point due to vacuum. Stripped ammonia is absorbed to a sulfuric acid solution, forming ammonium sulfate crystals as a marketable product. Three common types of digestate were found to have boiling point temperature-vacuum curves similar to water. Seven combinations of boiling temperature and vacuum (50 °C 16.6 kPa, 58 °C 20.0 kPa, 65 °C 25.1 kPa, 70 °C 33.6 kPa, 80 °C 54.0 kPa, 90 °C 74.2 kPa, and 100 °C 101.3 kPa) were tested for batch stripping of ammonia in dairy manure digestate. 93.3-99.9% of ammonia was stripped in 3 h. The Lewis-Whitman model fitted ammonia stripping process well. Ammonia mass transfer coefficient was significantly higher at boiling temperature 65-100 °C and vacuum pressure 25.1-101.3 kPa than 50-58 °C and 16.6-20.0 kPa. The low ammonia saturation concentrations (0-24 mg N/L) suggested a large driving force to strip ammonia. The optimum boiling point temperature - vacuum pressure for ammonia recovery in a recirculation line of a mesophilic digester was 65 °C and 25.1 kPa, at which the ammonia mass transfer coefficient was as high as 37.3 mm/h. Installation of a demister and liquid trap could avoid negative effects of higher stripping temperature and stronger vacuum on formation of ammonium sulfate crystals. Pilot tests demonstrated that high-purity ammonium sulfate crystals could be produced by controlling sulfuric acid content and maintaining acid solution saturated with ammonium sulfate. Although volatile organic compounds such as cyclohexene were found in the final acid solutions, no volatile organic compounds were found in the recovered crystals.

摘要

为了防止富含蛋白质的底物在厌氧消化过程中乙酸型产甲烷菌受到氨的抑制,需要从消化液中去除或回收氨。本文提出了一种将真空热汽提与酸吸收相结合的创新氨回收工艺。由于真空的作用,消化液在低于正常沸点的温度下沸腾,氨被汽提出来。汽提出来的氨被吸收到硫酸溶液中,形成硫酸铵晶体作为有市场价值的产品。三种常见类型的消化液的沸点-真空曲线与水相似。对 7 种不同的沸腾温度和真空度组合(50°C、16.6kPa;58°C、20.0kPa;65°C、25.1kPa;70°C、33.6kPa;80°C、54.0kPa;90°C、74.2kPa;100°C、101.3kPa)进行了批处理汽提实验,以研究其在奶牛粪污消化液中脱氨的效果。在 3 小时内,氨的去除率为 93.3%-99.9%。Lewis-Whitman 模型很好地拟合了氨汽提过程。在 65-100°C 的沸腾温度和 25.1-101.3kPa 的真空压力下,氨传质系数明显高于 50-58°C 和 16.6-20.0kPa。低的氨饱和浓度(0-24mg N/L)表明有很大的驱动力来汽提氨。在中温消化器循环管路中,氨回收的最佳沸点-真空压力为 65°C 和 25.1kPa,此时氨传质系数高达 37.3mm/h。安装除雾器和液体捕集器可以避免更高的汽提温度和更强的真空对硫酸铵晶体形成的负面影响。中试表明,通过控制硫酸含量并保持硫酸铵饱和的酸溶液,可以生产出高纯度的硫酸铵晶体。尽管最终的酸溶液中发现了环己烯等挥发性有机化合物,但在回收的晶体中没有发现挥发性有机化合物。

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