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Granular Sludge Bed

  • Biofilter: Expanded Granular Sludge Bed

    EGSB. An extended granular sludge bed reactor (EGSB) is a variant of the UASB concept (Kato et al. 1994). The differentiating feature is that a higher upward flow velocity is provided for the wastewater passing through the sludge bed.

    EGSB Reactor

    The increased flow allows partial expansion (fluidization) of the granular sludge bed, improving contact between wastewater and sludge and promoting the segregation of small inactive suspended particles from the sludge bed. The increased flow rate is achieved either through the use of high reactors or through wastewater recirculation (or both).

    The EGSB concept is suitable for poorly soluble wastewater (less than 1 to 2 g of soluble COD /l) or for wastewater that contains inert or poorly biodegradable suspended solids that must not be deposited in the sludge bed.

    Overview of the performance of the reactors. A recent survey (Frankin, 2001) carefully documented 1215 large-scale, high-speed anaerobic reactors built around the world since the 1970s to treat industrial wastewater. The overwhelming majority (72% of all plants) of existing large-scale plants are based on the UASB or EGSB concept developed by Lettinga in the Netherlands. This statistic highlights that the anaerobic granular sludge bed concept is the most successful for scale-up and implementation. The average design load of the UASB of 682 large-scale systems examined was 10 kg COD/m3.d.

    Note: COD stands for chemical oxygen demand and refers to the organic matter in wastewater, expressed as the weight of oxygen required to burn it completely. The average design load of the EGSB of 198 large-scale systems examined was 20 kg COD/m3.d. COD removal efficiency largely depends on the type of wastewater; however, the biodegradable COD removal efficiency is generally over 85 or even 90%.

    Biodegradable COD is sometimes expressed by the biological oxygen demand ( BOD ) parameter.

    The four main applications for high-load anaerobic reactor systems are:

    • Breweries and beverage industry
    • Distilleries and fermentation industry
    • food industry
    • pulp and paper.


    These four industries together account for 87% of applications. However, the applications of the technology are rapidly expanding, including the treatment of wastewater from the chemical and petrochemical industries, the textile industry, landfill leachate, as well as applications aimed at sulfur cycle conversion and metal removal (see Other Applications). In addition, the UASB concept is also suitable for the treatment of household wastewater in warm climates.


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    Wang, Xu & Ding, Jie & Ren, Nan-Qi & Liu, Bing-Feng & Guo, Wan-Qian. (2009). CFD simulation of an expanded granular sludge bed (EGSB) reactor for biohydrogen production. International Journal of Hydrogen Energy. 34. 9686-9695. 10.1016/j.ijhydene.2009.10.027. Understanding how a bioreactor functions is a necessary precursor for successful reactor design and operation. This paper describes a two-dimensional computational fluid dynamics simulation of three-phase gas–liquid–solid flow in an expanded granular sludge bed (EGSB) reactor used for biohydrogen production. An Eulerian–Eulerian model was formulated to simulate reaction zone hydrodynamics in an EGSB reactor with various hydraulic retention times (HRT). The three-phase system displays a very heterogeneous flow pattern especially at long HRTs. The core-annulus structure developed may lead to back-mixing and internal circulation behavior, which in turn gives poor velocity distribution. The force balance between the solid and gas phases is a particular illustration of the importance of the interphase rules in determining the efficiency of biohydrogen production. The nature of gas bubble formation influences velocity distribution and hence sludge particle movement. The model demonstrates a qualitative relationship between hydrodynamics and biohydrogen production, implying that controlling hydraulic retention time is a critical factor in biohydrogen-production.

    Image : http://ww25.uasb.org/


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  • Biofilter: Upward-flow Anaerobic Sludge Blanket

    Anaerobic granular sludge bed technology refers to a special reactor concept for the anaerobic treatment of wastewater with high throughput. The concept was introduced with the UASB reactor (UASB = upward-flow anaerobic sludge blanket). A schematic of a UASB reactor is shown in the figure.

    Schematic of the Upflow Anaerobic Sludge Blanket Reactor UASB

    From a hardware perspective, at first glance, a UASB reactor is nothing more than an empty tank (i.e. an extremely simple and inexpensive design).

    The wastewater is fed into the tank via appropriately arranged inlets. The wastewater flows upward through an anaerobic sludge bed where the microorganisms in the sludge come into contact with the wastewater substrates. The sludge bed consists of microorganisms that naturally form granules (pellets) with a diameter of 0.5 to 2 mm, which have a high sedimentation rate and are therefore not washed out of the system even under high hydraulic loads. The resulting anaerobic degradation process is usually responsible for the production of gas (e.g. biogas containing CH4 and CO2). The upward movement of the released gas bubbles causes hydraulic turbulence, which ensures mixing of the reactor without mechanical parts. At the top of the reactor, the water phase is separated from the sludge solids and gas in a three-phase separator (also called a gas-liquid solids separator). The three-phase separator is usually a gas cap with a settler above it. Baffles are used below the gas cap opening to direct the gas to the gas cap opening.

    Brief history of UASB

    The UASB procedure was developed by Dr. Gatze Lettinga and colleagues developed it in the late 1970s at Wageningen University (Netherlands). Inspired by publications by Dr. Perry McCarty (Stanford, USA), Lettinga's team experimented with an anaerobic filter concept. The Anaerobic Filter (AF) is a high-speed anaerobic reactor in which biomass is immobilized on an inert porous support material. During experiments with the AF, Lettinga observed that, in addition to the biomass fixed to the carrier material, a large part of the biomass developed into free granular aggregates. The UASB concept crystallized during Gatze Lettinga's trip to South Africa, where he observed the sludge developing into compact granules in an anaerobic wine vinasse treatment plant. The reactor design of the plant visited was a "Clarigestor", which can be considered a precursor to the UASB. The upper part of the "Clarigestor" reactor has a clarifier but no gas cap.

    The birth of the UASB

    The UASB concept emerged from the realization that an inert support material for biomass attachment is not necessary to maintain a high proportion of active sludge in the reactor. Instead, the UASB concept is based on a high degree of biomass retention through the formation of sludge granules. When developing the UASB concept, Lettinga took into account the need to promote the accumulation of granular sludge and prevent the accumulation of disperse sludge in the reactor. The most important features for the development of granular sludge are, firstly, maintaining an upward flow in the reactor that selects microorganisms to aggregate, and secondly, ensuring adequate separation of solids, liquid and gas to prevent leaching of the sludge grains.

    First UASB. The UASB reactor concept was quickly developed into technology, with the first pilot plant installed at a beet sugar refinery in the Netherlands (CSM suiker). Afterwards, a large number of large-scale systems were installed in sugar refineries, potato starch processing plants and other food industries as well as in waste paper factories in the Netherlands. The first publications on the UASB concept appeared in Dutch-language journals in the late 1970s, and the first international publication appeared in 1980 (Lettinga et al. 1980).

    Grahik: By Tilley, E., Ulrich, L., Lüthi, C., Reymond, Ph., Zurbrügg, C. - Compendium of Sanitation Systems and Technologies - (2nd Revised Edition). Swiss Federal Institute of Aquatic Science and Technology (Eawag), Duebendorf, Switzerland. ISBN 978-3-906484-57-0., CC BY-SA 3.0, https://commons.wikimedia.org/w/index.php?curid=42267210


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