4.5 Article

Ammonia recovery from human urine as liquid fertilizers in hollow fiber membrane contactor: Effects of permeate chemistry

期刊

ENVIRONMENTAL ENGINEERING RESEARCH
卷 26, 期 1, 页码 -

出版社

KOREAN SOC ENVIRONMENTAL ENGINEERS
DOI: 10.4491/eer.2019.523

关键词

Ammonia recovery; Fertilizer production; Human urine; Hollow-fiber membrane contactor

资金

  1. Korean government [20190278-001]
  2. Korea Environment Industry & Technology Institute (KEITI) through Industrial Facilities & Infrastructure Research Program - Korea Ministry of Environment(MOE), Republic of Korea [1485016257]

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The study investigated the recovery of ammonium fertilizers from human urine using liquid/liquid membrane contactor, with findings showing that the chemistry of the permeate side is a major factor affecting ammonia mass transfer. Sulfuric acid was found to be slightly better in capturing ammonia, and increasing acid concentration did not necessarily increase ammonia extraction tendency. The best operating pH for extracting ammonia for fertilizer purposes varied for different acid types.
The production of the existing nitrogen fertilizer is costly and less environmental-friendly. Various green technologies are currently emerging toward providing alternative options. In this study, a liquid/liquid hydrophobic hollow-fiber membrane contactor was employed at ambient temperature and natural urine pH similar to 9.7 to recover ammonium fertilizers from human urine. Results showed that permeate side chemistry was one of the major factors affecting the ammonia mass transfer. The study on the ammonia capturing performance of diluted sulfuric acid, phosphoric acid, nitric acid, and DI water confirmed that acid type, acid concentration, and permeate side operating pH were the most important parameters affecting the ammonia capturing tendency. Sulfuric acid was slightly better in capturing more ammonia than other acid types. The study also identified increasing acid concentration didn't necessarily increase ammonia mining tendency because there was always one optimum concentration value at which maximum ammonia extraction was possible. The best permeate side operating pH to extract ammonia for fertilizer purposes was selected based on the dissociation equilibrium of different types of acids. Accordingly, the analysis showed that the membrane process has to be operated at pH > 3 for sulfuric acid, between 3.5 to 11.5 for phosphoric acid, and above 0.5 for nitric acid so as to produce their respective high-quality liquid ammonium sulfate, ammonium monophosphate/diphosphate, and ammonium nitrate fertilizer. Therefore, permeate side acid concentration, pH, and acid type has to always be critically optimized before starting the ammonia mining experiment.

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