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Anaerobic digestion, use

Figure 26.8 Suspended growth anaerobic digestion using an upward flow anaerobic sludge blanket. Figure 26.8 Suspended growth anaerobic digestion using an upward flow anaerobic sludge blanket.
Figure 26.9 Attached growth anaerobic digestion using a fluidized anaerobic bed. Figure 26.9 Attached growth anaerobic digestion using a fluidized anaerobic bed.
A. Punal, L. Palazzotto, J.C. Bouvier, T. Conte, and J.P. Steyer. Automatic control of VFA in anaerobic digestion using a fuzzy logic based approach. In IWA VII Latin America Workshop and Symposium on Anaerobic Digestion, pages 126-133, Merida, Mexico, 2002. [Pg.199]

In cheese whey wastewater treatment, the low pH would also inhibit the metha-nogenic process as the free ammonia did in the anaerobic digestion using other substrates. Ghaly et al. [85] found that with pH control, the biogas production of... [Pg.128]

Vesvikar MS, Al-Dahhan M. Flow pattern visualization in a mimic anaerobic digester using CFD. Biotechnol Bioeng 2005 89(6) 719-32. [Pg.133]

Collins, L.J., Paskins, A.R., 1987. Measurement of trace concentrations of hydrogen in biogas from anaerobic digesters using an exhaled hydrogen monitor. Water Research 21 (12), 1567-1572. [Pg.294]

Yushina, Y, Hasegawa, J. Process performance comparison of membrane introduced anaerobic digestion using food-industry waste-water. Desalination, 1994, 98, 413-421. [Pg.402]

Ana.eroblc Digestion. Methane can be produced from water slurries of biomass by anaerobic digestion in the presence of mixed populations of anaerobes. This process has been used for many years to stabilize municipal sewage sludges for purposes of disposal. Presuming the biomass is all cellulose, the chemistry can be represented in simplified form as follows ... [Pg.17]

Gasification. Conversion of biomass to gaseous fuels can be accompHshed by several methods only two are used by the biomass energy industry (ca 1992). One is thermal gasification in which LHV gas, ie, producer gas, is produced. The other process is anaerobic digestion, which yields an MHVgas. [Pg.41]

Anaerobic ponds are loaded such that anaerobic conditions prevail throughout the Hquid volume. One of the major problems with anaerobic ponds is the generation of odors. The odor problem can frequentiy be eliminated by the addition of sodium nitrate at a dosage equal to 20% of the appHed oxygen demand. An alternative is the use of a stratified facultative lagoon, in which aerators are suspended 3 meters below the Hquid surface in order to maintain aerobic surface conditions, with anaerobic digestion occurring at the lower depths. [Pg.189]

An anaerobic digester is a no-recycle complete mix reactor. Thus, its performance is independent of organic loading but is controlled by hydraulic retention time (HRT). Based on kinetic theoiy and values of the pseudo constants for methane bac teria, a minimum HRT of 3 to 4 days is required. To provide a safety factor and compensate for load variation as indicated earlier, HRT is kept in the range 10 to 30 days. Thickening of feed sludge is used to reduce the tank volume required... [Pg.2228]

Recovery of Riologieal Conversion Products Biological conversion produces that can be derived from solid wastes include compost, methane, various proteins and alcohols, and a variety of other intermediate organic compounds. The principal processes that have been used are reported in Table 25-64. Composting and anaerobic digestion, the two most highly developed processes, are considered further. The recovery of gas from landfills is discussed in the portion of this sec tion dealing with ultimate disposal. [Pg.2242]

Waste stabilization ponds are shallow basins into which wastes are fed for biological decomposition. The chemical reactions involved are the same as those that occur in the other biological processes. Aeration is provided by the wind, and anaerobic digestion may also occur near the bottom of deeper ponds. The ponds are very commonly used for sewage treatment and dilute industrial wastes. Waste stabilization ponds are normally used as the final treatment step for effluents because they are not effieient enough to be used on their own. [Pg.152]

These tanks at a water treatment facility are used to generate a mixture of methane and carbon dioxide by anaerobic digestion of sewage. The methane produced provides much of the power needed to run the facility. [Pg.368]


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Anaerobic digestion

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