Combined ammonia recovery and solid oxide fuel cell use at wastewater treatment plants for energy and greenhouse gas emission improvements

被引:34
作者
Grasham, Oliver [1 ,2 ]
Dupont, Valerie [1 ]
Alonso Camargo-Valero, Miller [3 ,4 ]
Garcia-Gutierrez, Pelayo [1 ]
Cockerill, Timothy [5 ]
机构
[1] Univ Leeds, Fac Engn, Sch Chem & Proc Engn, Leeds LS2 9JT, W Yorkshire, England
[2] Univ Leeds, Fac Engn, Ctr Doctoral Truining Bioenergy, Leeds LS2 9JT, W Yorkshire, England
[3] Univ Leeds, Sch Civil Engn, BioResource Syst Res Grp, Leeds LS2 9JT, W Yorkshire, England
[4] Univ Nacl Colombia, Dept Ingn Quim, Campus Nubia, Manizales, Colombia
[5] CIER, Leeds LS2 9JT, W Yorkshire, England
基金
英国工程与自然科学研究理事会;
关键词
Ammonia recovery; Wastewater treatment; Fuel Cell; Process modelling; Greenhouse gases; SOFC; PERFORMANCE; SYSTEM; SLUDGE; SIMULATION; MODEL; DEFINITION; SEPARATION; PARADIGM; BALANCES;
D O I
10.1016/j.apenergy.2019.02.029
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Current standard practice at wastewater treatment plants (WWTPs) involves the recycling of digestate liquor, produced from the anaerobic digestion of sludge, back into the treatment process. However, a significant amount of energy is required to enable biological breakdown of ammonia present in the liquor. This biological processing also results in the emission of damaging quantities of greenhouse gases, making diversion of liquor and recovery of ammonia a noteworthy option for improving the sustainability of wastewater treatment. This study presents a novel process which combines ammonia recovery from diverted digestate liquor for use (alongside biomethane) in a solid oxide fuel cell (SOFC) system for implementation at WWTPs. Aspen Plus V.8.8 and numerical steady state models have been developed, using data from a WWTP in West Yorkshire (UK) as a reference facility (750,000p.e.). Aspen Plus simulations demonstrate an ability to recover 82% of ammoniacal nitrogen present in digestate liquor produced at the WWTP. The recovery process uses a series of stripping, absorption and flash separation units where water is recovered alongside ammonia. This facilitates effective internal steam methane reforming in the fuel cell with a molar steam:CH4 ratio of 2.5. The installation of the process at the WWTP used as a case of study has the potential to make significant impacts energetically and environmentally; findings suggest the treatment facility could transform from a net consumer of electricity to a net producer. The SOFC has been demonstrated to run at an electrical efficiency of 48%, with NH3 contributing 4.6% of its power output It has also been demonstrated that 3.5 kg CO(2)e per person served by the WWTP could be mitigated a year due to a combination of emissions savings by diversion of ammonia from biological processing and lifecyde emissions associated with the lack of reliance on grid electricity.
引用
收藏
页码:698 / 708
页数:11
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