Abstract: Terylene artificial silk printing and dyeing wastewater (TPD
wastewater), containing averaged 710 mg/L terephthalic acid (TA) as the main
carbon source and the character pollutant, was subjected to expanded granular
sludge bed (EGSB) process. The stability of theEGSB process was firstly
conducted by laboratory experiment. TA ionization was the predominated factor
influencing the acid-base balance of the system. High concentration of TA in
wastewater resulted in sufficient buffering capacity to neutralize the volatile
fatty acids (VFA) generated from substrate degradation and provided strong base
for anaerobic system to resist the pH decrease below 6.5. VFA and UFA caused
almost no inhibition on the anaerobic process and biogas production except that
pH was below 6.35 and VFA was at its maximum value. Along with the granulating
of the activated sludge, the efficiency of organic removal and production rate
of biogas increased gradually and became more stable. After start-up, the
efficiency of COD removal increased to 57%–64%, pH stabilized in a range of
7.99–8.04, and production rate of biogas was relatively high and stable. Sludge
granulating, suitable influent of pH and loading were responsible for the EGSB
stability. The variation of VFA concentration only resulted in neglectable
rebound of pH, and the inhibition from VFA could be ignored in EGSB. The EGSB
reactor was stable for TPD wastewater treatment.