Treatment costs of ammonia recovery from biogas digestate by air stripping analyzed by process simulation

被引:34
作者
Errico, Massimiliano [1 ]
Sotoft, Lene Fjerbaek [1 ]
Nielsen, Anne Kjaerhuus [2 ]
Norddahl, Birgir [1 ]
机构
[1] Univ Southern Denmark, Dept Chem Engn Biotechnol & Environm Technol, Campusvej 55, DK-5230 Odense M, Denmark
[2] Renew Energy, Kullinggade 31E, DK-5700 Svendborg, Denmark
关键词
Air stripping; Ammonia recovery; Biogas digestate; Process simulation; PIG SLURRY;
D O I
10.1007/s10098-017-1468-0
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Ammonia can be recovered from liquid biogas digestate as ammonium sulfate by air stripping. A full-scale plant treating 30,000 kg h(-1) of digestate was simulated in Aspen Plus.The classical sequence stripper-absorber was modified by introducing a flash drum to reduce the buffer capacity. The stripped digestate was mixed with NaOH up to a pH value of 9 and fed to the stripping column using air at 90 A degrees C. The air flow rate was optimized considering the possible recycle from the absorption column. The complete process was modeled using the process simulator Aspen Plus considering a recovery of ammonia equal to 95%. The total capital investment was evaluated by means of Aspen Plus Process Economic Analyzer in about 5.5 million US$, and the costs of energy and chemicals were quantified in less than 1 million US$ year(-1). A benefit of 1.6 US$ for m(3) of digestate was obtained considering an ammonium sulfate price of 522 US$ ton(-1).
引用
收藏
页码:1479 / 1489
页数:11
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