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    Simulation and Control of Anaerobic Reactors

    , M.Sc. Thesis Sharif University of Technology Ghanavati, Mohammad Amin (Author) ; Shahrokhi, Mohammad (Supervisor) ; Vafa, Ehsan (Supervisor)
    Abstract
    Anaerobic digestion of waste and wastewater has attracted researchers’ attention due to its important effect on reducing greenhouse gas emissions and reducing the level of environmental pollution and production of methane as a renewable energy source. This process is highly sensitive and can become unstable due to the presence of complex biochemical reactions and containing various types of chemical in it. In order to understand and improve the performance of this process, modeling and design of an appropriate control strategy is needed. ADM1 is the most accurate model for this process which is used in this study to describe and simulate the anaerobic reactor. Constrained and unconstrained... 

    Simulation and Control of Anaerobic Reactors

    , M.Sc. Thesis Sharif University of Technology Ghanavati, Mohammad Amin (Author) ; Shahrokhi, Mohammad (Supervisor) ; Vafa, Ehsan (Supervisor)
    Abstract
    Anaerobic digestion of waste and wastewater has attracted researchers’ attention due to its important effect on reducing greenhouse gas emissions and reducing the level of environmental pollution and production of methane as a renewable energy source. This process is highly sensitive and can become unstable due to the presence of complex biochemical reactions and containing various types of chemical in it. In order to understand and improve the performance of this process, modeling and design of an appropriate control strategy is needed. ADM1 is the most accurate model for this process which is used in this study to describe and simulate the anaerobic reactor. Constrained and unconstrained... 

    Sulphate reduction in a three-stage packed-bed anaerobic bioreactor

    , Article World Environmental and Water Resources Congress 2008: Ahupua'a, Honolulu, HI, 12 May 2008 through 16 May 2008 ; Volume 316 , 2008 ; 9780784409763 (ISBN) Borghei, M ; Poorhashem, Q ; Environmental and Water Resources Institute of ASCE ; Sharif University of Technology
    2008
    Abstract
    In this paper the effect of the sulphate concentration on the performance of a three-stage anaerobic baffled packed-bed reactor (ABPR) was investigated. Synthetic wastewater (3000 mg COD/l) was used as the sole organic substrate. The 30 liters fixed-bed bioreactor filled with plastic packing and divided in three equal sections was used as the mABPR reactor. The unit was run at a hydraulic retention time (HRT) of 1 day and at temperature of 25° C. The results of this study showed that when COD/SO42- ratios were changed from 30 to 3 with increasing sulphate concentration from 100 to 1000 mg/l, COD removal slightly was decreased. Maximum COD and sulphate removal were 91 and 96%, respectively,... 

    Comparison of two mathematical models for correlating the organic matter removal efficiency with hydraulic retention time in a hybrid anaerobic baffled reactor treating molasses

    , Article Bioprocess and Biosystems Engineering ; Volume 35, Issue 3 , 2012 , Pages 389-397 ; 16157591 (ISSN) Ghaniyari Benis, S ; Martín, A ; Borja, R ; Martin, M. A ; Hedayat, N ; Sharif University of Technology
    Abstract
    A modelling of the anaerobic digestion process of molasses was conducted in a 70-L multistage anaerobic biofilm reactor or hybrid anaerobic baffled reactor with six compartments at an operating temperature of 26 °C. Five hydraulic retention times (6, 16, 24, 72 and 120 h) were studied at a constant influent COD concentration of 10,000 mg/L. Two different kinetic models (one was based on a dispersion model with first-order kinetics for substrate consumption and the other based on a modification of the Young equation) were evaluated and compared to predict the organic matter removal efficiency or fractional conversion. The first-order kinetic constant obtained with the dispersion model was... 

    Upgrading activated sludge systems and reduction in excess sludge

    , Article Bioresource Technology ; Volume 102, Issue 22 , November , 2011 , Pages 10327-10333 ; 09608524 (ISSN) Hazrati, H ; Shayegan, J ; Sharif University of Technology
    2011
    Abstract
    Most of 200 Activated Sludge Plant in Iran are overloaded and as a result, their efficiency is low. In this work, a pilot plant is manufactured and put into operation in one of the wastewater treatment plants in the west of Tehran. Instead of conventional activated sludge, a membrane bioreactor and an upflow anaerobic sludge blanket reactor used as a pretreatment unit in this pilot. For the sake of data accuracy and precision, an enriched municipal wastewater was opted as an influent to the pilot. Based on the attained result, the optimum retention time in this system was 4. h, and the overall COD removal efficiency was 98%. As a whole, the application of this retrofit would increase the...