Recovery of phosphorus, magnesium, and potassium from surplus activated sludge using existing sludge treatment facilities and thickened primary sludge

Author:

Kamiyama Yudai1,Shiraiwa Takuya1,Ishikawa Nao2,Takahashi Shinji3,Sasamoto Makoto4,Sasaki Masayuki5,Watanabe Toru6,Ito Ayumi2

Affiliation:

1. a Division of Regional Development and Creativity, Graduate School of Arts and Sciences, Iwate University, Ueda 4-3-5, Morioka 020-8551, Japan

2. b Course of Civil and Environmental Engineering, Department of System Innovation Engineering, Faculty of Science and Engineering, Iwate University, Ueda 4-3-5, Morioka 020-8551, Japan

3. c Graduate School of Engineering, Tohoku University, 6-6-11 Aramaki Aza Aoba, Aoba-ku, Sendai 980-8579, Japan

4. d Technical Office, Faculty of Science and Engineering, Iwate University, Ueda 4-3-5, Morioka 020-8551, Japan

5. e Iwate Prefectural Sewerage Public Cooperation, Higashi-Mirumae 3-10-2, Morioka 020-0832, Japan

6. f Department of Food, Life and Environmental Sciences, Faculty of Agriculture, Yamagata University, Wakaba-machi 1-23, Tsuruoka 997-8555, Japan

Abstract

Abstract The separation of P, K, and Mg from surplus activated sludge (SAS) was investigated using existing sludge treatment facilities and the thickened primary sludge (TPS). The addition of the TPS to the SAS storage tank accelerated the anaerobic release of the three elements from SAS with maximum efficiencies of about 60%. The efficiency of P release showed a significant correlation with the oxidation–reduction potential. Increasing the total solid concentration increased the release of elements. The released elements could be transferred to a separate liquid (SL) from a screw-press thickener, and maximum concentrations of P, K, and Mg were about 200, 60, and 35 mg/L, respectively. The addition of CaCl2 and NaOH solutions to SL precipitated P as hydroxyapatite. However, no precipitation of K and Mg occurred simultaneously with P, even when the pH of SL was increased to 9. These findings suggest that about 60% of P, K, and Mg can be separated from SAS into SL using existing sludge treatment facilities and TPS; however, a method other than precipitation would be needed to recover P and K from SL simultaneously.

Funder

Ministry of Land, Infrastructure, Transportation and Tourism of Japan

Fuso Innovative Technology Fund

Publisher

IWA Publishing

Reference24 articles.

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5. Accelerated anaerobic release of K, Mg and P from surplus activated sludge for element recovery and struvite formation inhibition;Water. Sci. Technol.,2017

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