Feeding control of anaerobic co-digestion of waste activated sludge and corn silage performed by rule-based PID control with ADM1

• Published in: Waste management (Elmsford) 2020-02, Vol.103, p.22-31
• Main Authors: Zhou, Haidong, Ying, Zhenxi, Cao, Zhengcao, Liu, Zhiyong, Zhang, Zhe, Liu, Weidong
• Format: Article
• Language: English
• Subjects: Anaerobiosis; Biofuels; Bioreactors; Co-substrate; Methane; Methane production; Proportional-integral-derivative control; Setpoint; Sewage; Silage; Volatile fatty acid; Zea mays
• ISSN: 0956-053X; 1879-2456
• DOI: 10.1016/j.wasman.2019.12.021

[Display omitted] •Rule-based PID control with adapted ADM1 built for anaerobic co-digestion (AcoD).•Maximal biogas production was 0.94 m3/kgVS·d at feeding ratio of CS to WAS 1:1.2.•Adapted ADM1 after calibration could precisely simulate AcoD of WAS and CS.•Control strategy was in cascade structure with additional rule-based expert system.•Control system improved resistance to AcoD disturbances and maximised CH4 production. Anaerobic co-digestion (AcoD) of corn silage (CS) and waste activated sludge (WAS) co-substrates, compared with anaerobic digestion (AD) of mono-substrate WAS, was simulated under mesophilic conditions with the adapted IWA Anaerobic Digestion Model No. 1 (ADM1), and a rule-based PID control system for control of the AcoD of CS and WAS, through control of their ratios in the feed, was developed, implemented with the model as a test platform. Tests on AcoD of co-substrates were conducted at the COD mass-based feeding ratios of CS to WAS 1:2.5, 1:2.0 and 1:1.2. The maximal biogas production was 0.94 m3/kgVS·d at the feeding ratio 1:1.2. The ADM1 was adapted, and the high-sensitivity kinetic parameters were calibrated and optimised using the data from the tests of steady state mono-digestion of WAS and AcoD of CS and WAS. The simulated data of biogas and methane production, methane content, VFA and pH agreed well with the test data. The rule-based PID control was developed with an additional expert system, in which the lower level controller operated the level of VFA/TIC and the upper level controller manipulated the setpoints of methane production. The feeding ratio of CS to WAS was used as a manipulated variable. With the constraint boundaries, the test on the control system showed that it could keep methane production stable to the setpoint and maximise methane production while resisting the disturbances to AcoD by adjusting the feeding ratios of CS to WAS.