This paper presents the results obtained for the effluent dewatering properties of anaerobic digestion of secondary sludge （SS） and anaerobic co-digestion of mixture of this sludge with the distillery wastewater （D...This paper presents the results obtained for the effluent dewatering properties of anaerobic digestion of secondary sludge （SS） and anaerobic co-digestion of mixture of this sludge with the distillery wastewater （DW） under thermophilic （55±1 ℃）, 5 L of working volume, three parallel lab-scale conditions. Its mixtures were prepared with a DW content of 25%and 50% and the C/N ratios of mixtures are 13.1 and 17.6, respectively. The effluent dewatering properties were evaluated under stable conditions which the biogas yield and the effluent pH were steady. The natural settleability, biogas yield, centrifugal dewatering, centrifugal supernatant turbidity and specific resistance filtration （SRF） were investigated. The results showed that the effluent dewatering properties of anaerobic co-digestion of mixtures between SS and DW were better than that of anaerobic digestion of SS alone. In the anaerobic digestion system with the feed were SS, mixture of SS and a DW content of 25%and 50% in order, the net biogas yield of secondary sludge in ADSA,ADSB and ADSC were 0.42 0.507 and 0.511 m3 biogass/kg.VS.d ; compared with the biogas yield in anaerobic digestion system A （ADSA）, the biogas yield in anaerobic digestion system B （ADSB） and anaerobic digestion system C （ADSC） had been increased by more than 20% respectively; the SRF of three digested sludge are（were） from 6.8×10^13, 1. 1×10^13 to 5.1×10^12 m/Kg, natural settling rates of 12 h are 26, 37 and 56% and that of 24 h are 32%, 45% and 59% respectively; the centrifugal dewatering rate of 3 min at speed of 1000 rpm were 16%, 31% and 51% respectively; the turbidity of centrifugal supernatant were 804, 754 and 678FTU simultaneously.展开更多
An aerobic composting method is studied to reuse organic waste from rubb er factory waste as soil fertilizer and to study the effect of cellulolytic microbial activator （CMA） as the activator in the rubber factory w...An aerobic composting method is studied to reuse organic waste from rubb er factory waste as soil fertilizer and to study the effect of cellulolytic microbial activator （CMA） as the activator in the rubber factory waste composting. The performance of the composting process was monitored as a function of carbon and organic matter decomposition rate, temperature and moisture content. The results indicate that the rubber factory waste is best composted with water hyacinth and sludge than composted alone. In addition, the CMA is more aft^ctive when mixed with the rubber factory waste, water hyacinth and sludge since a good fertilizer is achieved. When adding CMA into the rubber factory waste composted alone, the finished product does not achieve a standard of fertilizer, especially the C/N ratio. The finished products （both CMA and without CMA）, can be an environmental friendly alternative to solve the disposal problems of rubber factory waste, Since the C/N ratio, pH, moisture content, temperature, and nutrients of the finished products are acceptable for agriculture use.展开更多
This paper presents bench scale experiments related to anaerobic co-digestion of aerobic sewage sludge from a pilot WWTP （waste water treatment plants）, raw glycerol from a biodiesel industry and food waste. Assays ...This paper presents bench scale experiments related to anaerobic co-digestion of aerobic sewage sludge from a pilot WWTP （waste water treatment plants）, raw glycerol from a biodiesel industry and food waste. Assays were conducted in 100 mL non-stirring penicillin vessels, at 30 ℃ and planned according to three optimization phases： （1） binary mixture of sewage sludge and FW （food waste）; （2） binary mixture of sewage sludge and glycerol; and （3） ternary mixture of sewage sludge, FW, and glycerol. In the first and second phases, the highest SMP （specific methane production） was achieved by 10% （v/v） FW and 0.5% （v/v） glycerol mixtures. The optimization of the ternary mixture during the third phase was reached by the combination of 10% （v/v） FW and 0.4% （v/v） glycerol. Despite the low SMP value, the addition of glycerol and FW contributed to doubling the SMP value of the sludge sample control.展开更多
文摘This paper presents the results obtained for the effluent dewatering properties of anaerobic digestion of secondary sludge （SS） and anaerobic co-digestion of mixture of this sludge with the distillery wastewater （DW） under thermophilic （55±1 ℃）, 5 L of working volume, three parallel lab-scale conditions. Its mixtures were prepared with a DW content of 25%and 50% and the C/N ratios of mixtures are 13.1 and 17.6, respectively. The effluent dewatering properties were evaluated under stable conditions which the biogas yield and the effluent pH were steady. The natural settleability, biogas yield, centrifugal dewatering, centrifugal supernatant turbidity and specific resistance filtration （SRF） were investigated. The results showed that the effluent dewatering properties of anaerobic co-digestion of mixtures between SS and DW were better than that of anaerobic digestion of SS alone. In the anaerobic digestion system with the feed were SS, mixture of SS and a DW content of 25%and 50% in order, the net biogas yield of secondary sludge in ADSA,ADSB and ADSC were 0.42 0.507 and 0.511 m3 biogass/kg.VS.d ; compared with the biogas yield in anaerobic digestion system A （ADSA）, the biogas yield in anaerobic digestion system B （ADSB） and anaerobic digestion system C （ADSC） had been increased by more than 20% respectively; the SRF of three digested sludge are（were） from 6.8×10^13, 1. 1×10^13 to 5.1×10^12 m/Kg, natural settling rates of 12 h are 26, 37 and 56% and that of 24 h are 32%, 45% and 59% respectively; the centrifugal dewatering rate of 3 min at speed of 1000 rpm were 16%, 31% and 51% respectively; the turbidity of centrifugal supernatant were 804, 754 and 678FTU simultaneously.
文摘An aerobic composting method is studied to reuse organic waste from rubb er factory waste as soil fertilizer and to study the effect of cellulolytic microbial activator （CMA） as the activator in the rubber factory waste composting. The performance of the composting process was monitored as a function of carbon and organic matter decomposition rate, temperature and moisture content. The results indicate that the rubber factory waste is best composted with water hyacinth and sludge than composted alone. In addition, the CMA is more aft^ctive when mixed with the rubber factory waste, water hyacinth and sludge since a good fertilizer is achieved. When adding CMA into the rubber factory waste composted alone, the finished product does not achieve a standard of fertilizer, especially the C/N ratio. The finished products （both CMA and without CMA）, can be an environmental friendly alternative to solve the disposal problems of rubber factory waste, Since the C/N ratio, pH, moisture content, temperature, and nutrients of the finished products are acceptable for agriculture use.
文摘This paper presents bench scale experiments related to anaerobic co-digestion of aerobic sewage sludge from a pilot WWTP （waste water treatment plants）, raw glycerol from a biodiesel industry and food waste. Assays were conducted in 100 mL non-stirring penicillin vessels, at 30 ℃ and planned according to three optimization phases： （1） binary mixture of sewage sludge and FW （food waste）; （2） binary mixture of sewage sludge and glycerol; and （3） ternary mixture of sewage sludge, FW, and glycerol. In the first and second phases, the highest SMP （specific methane production） was achieved by 10% （v/v） FW and 0.5% （v/v） glycerol mixtures. The optimization of the ternary mixture during the third phase was reached by the combination of 10% （v/v） FW and 0.4% （v/v） glycerol. Despite the low SMP value, the addition of glycerol and FW contributed to doubling the SMP value of the sludge sample control.
