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bottom section help add_ together significant biomass inventories which leads to increase process stability and higher removal. The cross flow media modules also function as effective gas-liquid-solids separator further enhancing biomass retention. Fig. 1: Upflow Hybrid Anaerobic Filter [77] The systems can be further qualified based on process rate, which were low-rate systems and high rate systems. Thus one can have low-rate with suspended-growth anaerobic system which includes bulk volume reactors and anaerobic contact reactors. Both these approaches are efficient at retaining flocculent (i.e. non-granular) sludge owing to lower organic and hydraulic loading rates than the high-rate systems. Particularly they are very well suited for industrial applications that do not granulate well or have higher than desirable amounts of troublesome constituents, example as high levels of organic and suspended solids. The systems can be further qualified based on process rate,

Figure 1 bottom section help add_ together significant biomass inventories which leads to increase process stability and higher removal. The cross flow media modules also function as effective gas-liquid-solids separator further enhancing biomass retention. Fig. 1: Upflow Hybrid Anaerobic Filter [77] The systems can be further qualified based on process rate, which were low-rate systems and high rate systems. Thus one can have low-rate with suspended-growth anaerobic system which includes bulk volume reactors and anaerobic contact reactors. Both these approaches are efficient at retaining flocculent (i.e. non-granular) sludge owing to lower organic and hydraulic loading rates than the high-rate systems. Particularly they are very well suited for industrial applications that do not granulate well or have higher than desirable amounts of troublesome constituents, example as high levels of organic and suspended solids. The systems can be further qualified based on process rate,

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Gas formation problem can be minimized by employing vacuum degasification and applying thermal shock prior to sedimentation using flocculating agents in settling tank incorporating inclined plates into the settler design. Although simple in concept, individual units make ACP more complex than other high rate ADs. Absence of any internal fittings offers some advantages for the treatment of wastes having high solids content. Anaerobic contact reactors employ an external clarifier or vessel to settle solids and consequently recycle them back to the reactor tank. Ty pical configurations include large tanks due to the Ow hydraulic and organic loading rates employed in their design. Anaero granulation is difficult or wastewater contains higher t desirab bic contact systems are particularly efficient w. e amounts of troublesome constituents, such nen nan as suspended solids. Anaerobic contact alternatives are effective at SUCCESS. fully retaining flocculent, such as non-granular slud ge,
Gas formation problem can be minimized by employing vacuum degasification and applying thermal shock prior to sedimentation using flocculating agents in settling tank incorporating inclined plates into the settler design. Although simple in concept, individual units make ACP more complex than other high rate ADs. Absence of any internal fittings offers some advantages for the treatment of wastes having high solids content. Anaerobic contact reactors employ an external clarifier or vessel to settle solids and consequently recycle them back to the reactor tank. Ty pical configurations include large tanks due to the Ow hydraulic and organic loading rates employed in their design. Anaero granulation is difficult or wastewater contains higher t desirab bic contact systems are particularly efficient w. e amounts of troublesome constituents, such nen nan as suspended solids. Anaerobic contact alternatives are effective at SUCCESS. fully retaining flocculent, such as non-granular slud ge,
These materials have exceptionally high surface area to volume ratios (400 m’/m’) and low void volumes. Its resistance to shock loads and inhibitions make anaerobic filter suitable for the treatment of both high strength and dilute wastewaters. Restrictions of anaerobic filter are mostly physical ones related to deterioration of the bed structure through a gradual accumulation of non-biodegradable solids. This leads eventually to short circuiting and channeling flow, and anaerobic filters are therefore unsuitable for wastewaters with high solids contents. Additionally, there is a relatively high cost due to the packing materials [5].
These materials have exceptionally high surface area to volume ratios (400 m’/m’) and low void volumes. Its resistance to shock loads and inhibitions make anaerobic filter suitable for the treatment of both high strength and dilute wastewaters. Restrictions of anaerobic filter are mostly physical ones related to deterioration of the bed structure through a gradual accumulation of non-biodegradable solids. This leads eventually to short circuiting and channeling flow, and anaerobic filters are therefore unsuitable for wastewaters with high solids contents. Additionally, there is a relatively high cost due to the packing materials [5].
located in lower part of reactor, while upper part contains a three phase separation system, which are the most characteristic feature of UASB reactor (Figure 4).
located in lower part of reactor, while upper part contains a three phase separation system, which are the most characteristic feature of UASB reactor (Figure 4).
Fig. 5: Anaerobic Baffled Reactors [1].
Fig. 5: Anaerobic Baffled Reactors [1].
Related topics:
Anaerobic DigestionBiological Wastewater Treatment
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