A new insight into the low membrane fouling tendency of liquid-liquid hollow fiber membrane contactor capturing ammonia from human urine

To unravel the low membrane fouling tendency and underlying membrane fouling mechanism of liquid-liquid hollow fiber membrane contactor (LL-HFMC) capturing ammonia from human urine, the ammonia flux decline trend, membrane fouling propensity, foulant-membrane thermodynamic interaction energy and micro-scale force analysis at different feed urine pH were comprehensively investigated. The 21-d continuous experi-ments showed that the ammonia flux decline trend and membrane fouling propensity significantly strengthened with the decrease of feed urine pH. The calculated foulant-membrane thermodynamic interaction energy decreased with the decreasing feed urine pH and agreed with the ammonia flux decline trend and membrane fouling propensity. The microscale force analysis showed that the absence of hydrodynamic water permeate drag force resulted in the foulant located at long distance from the membrane were difficult to approach the mem-brane surface, thus considerably alleviating membrane fouling. Additionally, the vital thermodynamic attractive force near the membrane surface increased with the decrease of feed urine pH, which made the membrane fouling further relieved at high pH condition. Therefore, the absence of water permeate drag force and operating at high pH condition minimized the membrane fouling during the LL-HFMC ammonia capture process. The obtained results provide a new insight into the low membrane tendency mechanism of LL-HFMC.

Automated summary

A comprehensive investigation was conducted to unravel the low membrane fouling tendency and underlying mechanism of liquid-liquid hollow fiber membrane contactor (LL-HFMC) for capturing ammonia from human urine. The results showed that the ammonia flux decline trend and membrane fouling propensity significantly strengthened with the decrease of feed urine pH. This was consistent with the decrease in foulant-membrane thermodynamic interaction energy. Microscale force analysis revealed that the absence of hydrodynamic water permeate drag force and operating at high pH condition minimized the membrane fouling during the LL-HFMC ammonia capture process.