Biogas Plasticization Coupled Anaerobic Digestion: Anaerobic Pump Calorimetry.

This paper presents the quantitative bomb calorimetric high heat values (HHV) for residue samples collected from the Anaerobic Pump (®TAP) and a continuous flow stirred tank reactor (CFSTR) anaerobically digesting a 50:50 wastewater sludge substrate. TAP, an advanced anaerobic digestion (AD) process, features biogas plasticization that greatly increases gas production and leaves a mineralized residual. Measured residue HHVs are compared to HHV estimates from literature empirical relationships. Two empirical formulations, the Meraz thermodynamic formulation (with 7.4% moisture) (Meraz et al. The Chemical Educator, 7(2), 66-70, (2002) and the Channiwala Universal formulation (Channiwala et al. Fuel, 81(8), 1051-1063, (2002), compared favorably (within ± 3% mean value) with the bomb measured HHV values. A stoichiometric ICC description for Ucells is derived. The thermodynamic formation potentials of all measured residues are derived including Ucells. An empirical method was used to calculate the entropy of formation (∆fS) for all residues and Ucells. Krevelen plots show residue molar ratios of oxygen and hydrogen to carbon (H/C, O/C) are linearly correlated with HHV and formation potentials (∆fG', ∆fH', ∆fS') with strong statistical coefficients of determination (R2). Residue H/C and O/C ratios fell across the peat classification on the biomass coalification diagram. A wide AD methane fermentation zone ≤ 18.6 MJ/kg is identified. The methods and correlation relationships presented enable the computation of accurate HHV and thermodynamic formation potentials without the necessity of direct thermal measurement. These quantitative results confirm that steady state AD of a well-known heterogeneous solid substrate (WWTP sludge) is a linear thermodynamic process.

Biogas plasticization coupled anaerobic digestion: the anaerobic pump stoichiometry.

This paper presents the stoichiometry section of a bioenergetics investigation into the biogas plasticization of wastewater sludge using the Anaerobic Pump (TAP). Three residue samples, an input substrate and two residual products, were collected from two side by side operated AD systems, a conventional continuous flow and stirred reactor, and TAP, and submitted for elemental and calorimetric analyses. The elemental compositions of the residues were fitted to a heterotrophic metabolism model [1] for both systems. To facilitate balanced stoichiometric models, a simple "cell" correction computation separates measured residual composites into "real" residual composition and cell growth (C5H7NO2) components. The elemental data and model results show that the TAP stage II residual composition (C1H0.065O0.0027N0.036) was nearly devoid of hydrogen and oxygen, leaving only fixed carbon and cells grown as the composition of the remaining mass. This quantitative evidence supports prior measurements of very high methane yields from TAP stage II reactor during steady-state experiments [2]. All performance parameters derived from the stoichiometric model(s) showed good agreement with measured steady-state averaged values. These findings are strong evidence that plasticization-disruption (TAP) cycle is the mechanism responsible for the observed increases in methane yield. The accuracy achieved by the stoichiometry models qualifies them for thermodynamic analysis to obtain potentials and bioconversion efficiencies. How applied pressure causes matrix conformation changes triggered by a functional consequence (plasticization and disruption) is this study's essential focus.

Biogas plasticization coupled anaerobic digestion: continuous flow anaerobic pump test results.

In this investigation, the Anaerobic Pump (TAP) and a conventional continuous flow stirred tank reactor (CFSTR) were tested side by side to compare performance. TAP integrates anaerobic digestion (AD) with biogas plasticization-disruption cycle to improve mass conversion to methane. Both prototypes were fed a "real world" 50:50 mixture of waste-activated sludge (WAS) and primary sludge and operated at room temperature (20 degrees Celsius). The quantitative results from three steady states show TAP peaked at 97% conversion of the particulate COD in a system hydraulic residence time (HRT) of only 6 days. It achieved a methane production of 0.32 STP cubic meter CH(4) per kilogram COD fed and specific methane yield of 0.78 m(3) CH(4) per cubic meter per day. This was more than three times the CFSTR specific methane yield (0.22 m(3) CH(4) per cubic meter per day) and more than double the CFSTR methane production (0.15 m(3) CH(4) per kilogram COD fed). A comparative kinetics analysis showed the TAP peak substrate COD removal rate (R (o)) was 2.24 kg COD per cubic meter per day, more than three times the CFSTR substrate removal rate of 0.67 kg COD per cubic meter per day. The three important factors contributing to the superior TAP performance were (1) effective solids capture (96%) with (2) mass recycle and (3) stage II plasticization-disruption during active AD. The Anaerobic Pump (TAP) is a high rate, high efficiency-low temperature microbial energy engine that could be used to improve renewable energy yields from classic AD waste substrates like refuse-derived fuels, treatment plant sludges, food wastes, livestock residues, green wastes and crop residuals.

Biogas plasticization coupled anaerobic digestion: batch test results.

Biogas has unique properties for improving the biodegradability of biomass solids during anaerobic digestion (AD). This report presents batch test results of the first investigation into utilizing biogas plasticization to "condition" organic polymers during active digestion of waste activated sludge (WAS). Preliminary design calculations based on polymer diffusion rate limitation are presented. Analysis of the 20 degrees C batch test data determined the first order (k(1)) COD conversion coefficient to be 0.167 day(-1) with a maximum COD utilization rate of 11.25 g L(-1) day(-1). Comparison of these batch test results to typical conventional AD performance parameters showed orders of magnitude improvement. These results show that biogas plasticization during active AD could greatly improve renewable energy yields from biomass waste materials such as MSW RDF, STP sludges, food wastes, animal manure, green wastes, and agricultural crop residuals.