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    Optimization of Mucor miehei rennin production and recovery

    , Article Scientia Iranica ; Volume 9, Issue 1 , 2002 , Pages 99-104 ; 10263098 (ISSN) Kazemi Vaysari, A ; Kheirolomoom, A ; Arjmand, M ; Habibollahi, M ; Sharif University of Technology
    Sharif University of Technology  2002
    Abstract
    In this paper, fungal rennin production has been carried out by solid state fermentation of Mucor miehei NRRL 3420. The optimum dilution ratio, temperature and fermentation time of the enzymatic solution were determined to be 1:30, 40°C and 4 days after the beginning of the fermentation process, respectively. Also, the enzyme recovery by precipitation was studied using (NH4)2SO4, acetone and ethanol, respectively. The effects of pH, salt and solvent concentration on rennin recovery were studied and the optimum pH value as well as the optimum salt concentration were determined. The maximum specific activity of the enzyme was obtained by precipitation at pH of 6.5 and 50% saturated solution of... 

    Ethanol production from sugarcane bagasse by means of on-site produced and commercial enzymes; A comparative study

    , Article Periodica Polytechnica: Chemical Engineering ; Volume 56, Issue 2 , 2012 , Pages 91-96 ; 03245853 (ISSN) Shaibani, N ; Yaghmaei, S ; Andalibi, M. R ; Ghazvini, S ; Sharif University of Technology
    2012
    Abstract
    In this study ethanol was produced without using expensive commercial enzymes from sugarcane bagasse. Alkali pretreatment was used to prepare biomass before enzymatic hydrolysis. The comparison between NaOH, KOH and Ca(OH)2 revealed that NaOH has been more effective on bagasse structure. The required enzymes for biomass hydrolysis were produced by bagasse solid state fermentation using three fungi: Trichoderma longibrachiatum, T. reesei and Aspergillus niger. Results indicated enzyme solution produced by A. niger has functioned better than the other two in cellulose conversion during sole hydrolysis. Ethanol was produced by simultaneous saccharification and fermentation (SSF) with on-site... 

    Xylanase production under solid state fermentation by aspergillus niger

    , Article International Journal of Engineering, Transactions B: Applications ; Volume 24, Issue 3 , March , 2011 , Pages 197-208 ; 1728-144X (ISSN) Shahi, S. S ; Alemzadeh, I ; Khanahmadi, M ; Roostaazad, R ; Sharif University of Technology
    Materials and Energy Research Center  2011
    Abstract
    Central composite orthogonal design was applied to quantify relations of xylanase production, loss of dry matter and change of pH with four critical variables during solid state fermentation of a mixture of wheat bran and wheat straw on which Aspergillus niger CCUG 33991 was cultivated. The studied variables included the percentage of wheat straw, wheat bran, temperature, moisture content, and fermentation time. The second-order quadratic model predicted the xylanase activity at a suitable set of conditions namely 29°C, 55% moisture content, and 50 hours of fermentation to be 1465 U/g of fermented dry matter which differed less than 6% from measured value at this set of conditions.... 

    Bed moisture estimation by monitoring of air stream temperature rise in packed-bed solid-state fermentation

    , Article Chemical Engineering Science ; Volume 61, Issue 17 , 2006 , Pages 5654-5663 ; 00092509 (ISSN) Khanahmadi, M ; Roostaazad, R ; Mitchell, D. A ; Miranzadeh, M ; Bozorgmehri, R ; Safekordi, A ; Sharif University of Technology
    2006
    Abstract
    We develop a method for predicting the moisture content of the fermenting solids in an intermittently mixed packed-bed bioreactor on the basis of measurements of the inlet and outlet gas stream temperatures and the assumption that both the gas streams are saturated with water vapor. This method can be used to estimate when an intermittently mixed packed bed should be mixed and how much water should be added during the mixing event. The predictions were experimentally verified for the growth of Aspergillus niger on wheat bran in a thin packed bed. We show that the application of a controller based on our estimation method would have led to adequate moisture control, with significant errors in... 

    Kinetic measurements for pseudomonas aeruginosa mr01 during biosurfactant production in two-phase system and developing a double-exponential model for viable cell profile

    , Article World Applied Sciences Journal ; Volume 22, Issue 6 , 2013 , Pages 809-816 ; 18184952 (ISSN) Bagheri Lotfabad, T ; Tayyebi, S ; Roostaazad, R ; Sharif University of Technology
    2013
    Abstract
    Biosurfactants are microbial substances which influence interfacial tension. The kinetic study was carried out for Pseudomonas aeruginosa MR01 during biosurfactant production in a two-phase liquid-liquid batch fermentation system. The maximum rhamnolipid concentration (Pmax) and the yield of biosurfactant per 1 biomass (YP/X) in a 5-L bioreactor containing soybean oil medium were found to be approximately 20.9 g.L and 3.1 g.g-1, respectively. Previously reported kinetic models in aqueous systems, three-parameter Gompertz, 2 Luedeking-Piret and Mercier equations, demonstrated adequate goodness-of-fit (r >0.9) to kinetic data recorded for biomass growth, nitrate consumption and rhamnolipid... 

    Optimization of microbial culture for production of poly hydroxy butyrate (PHB) by azotobacter beijerinckii DSMZ-1041

    , Article World Applied Sciences Journal ; Volume 14, Issue SPL ISS 3 , 2011 , Pages 72-82 ; 18184952 (ISSN) Montaser, N ; Ardjmand, M ; Nasab, A. H ; Kordi, A. S ; Sharif University of Technology
    Abstract
    Azotobacter beijerinckii DSMZ 1041 strain was used for production of polyhydroxybutyrate (PHB) and the optimum glucose concentration, as the carbon source and ammonium chloride, as the nitrogen source were obtained 60gr/lit and 0.5gr/lit respectively. The resulting optimum PHB production was investigated 2.95gr/lit. The obtained yield of PHB with respect to glucose (Yp/s) and PHB productivity (Qp) were 0.202 g/g and 0.123 g/lit.hr, respectively. The response surface methodology (RSM) was used to verify the accuracy of the designed experiments. azotobacter beijerinckii microorganism from Deutsch sammlung von microorganismen und zellkulturen(DSMZ) bank is used for production of Poly Hydroxy... 

    Investigation of optimum fermentation condition for PHA production by four species: Hydrogenophaga pseudoflava DSMZ 1034, azohydromonas lata DSMZ 1123, cupriavidus necator DSMZ 545, Azotobacter beijinckii DSMZ 1041

    , Article World Applied Sciences Journal ; Volume 14, Issue SPL ISS 3 , 2011 , Pages 36-47 ; 18184952 (ISSN) Karbasi, F ; Ardjmand, M ; Yunesi, H ; Safe Kordi, A ; Yaghmaei, S ; Sharif University of Technology
    2011
    Abstract
    Batch cultures of Azohydromonas lata DSMZ 1123, Hydrogenophaga pseudoflava DSMZ 1034, Cupriavidus necator DSMZ 545 and Azotobacter beijinckii DSMZ 1041 were investigated for producing the intracellular bioplastic poly-•-hydroxybutyrate (PHB). The effects of temperature, seed age, type of carbon sources and the agitation rate on the production rate of PHB were investigated using four mentioned spices. The optimized shaking rate, temperature and seed age were obtained 250 rpm, 30°C and 15 hrs for H. pseudoflava DSMZ 1034 and A. beijerinckii DSMZ 1041 and 18 hrs and 24 hrs for A. lata DSMZ 1123 and C. necator DSM 545, respectively.The effect of carbon sources including glucose, fructose, whey... 

    Fault diagnosis in a yeast fermentation bioreactor by genetic fuzzy system

    , Article Iranian Journal of Chemistry and Chemical Engineering ; Volume 29, Issue 3 , 2010 , Pages 61-72 ; 10219986 (ISSN) Tayyebi, S ; Shahrokhi, M ; Bozorgmehry Boozarjomehry, R ; Sharif University of Technology
    Abstract
    In this paper, the fuzzy system has been used for fault detection and diagnosis of a yeast fermentation bioreactor based on measurements corrupted by noise. In one case, parameters of membership functions are selected in a conventional manner. In another case, using certainty factors between normal and faulty conditions the optimal values of these parameters have been obtained through the genetic algorithm. These two cases are compared based on their performances in fault diagnosis of a yeast fermentation bioreactor for three different conditions. The simulation results indicate that the fuzzy-genetic system is superior in multiple fault detection for the conditions where the minimum and... 

    Comparison of solid substrate and submerged fermentation for chitosan production by aspergillus niger

    , Article Scientia Iranica ; Volume 17, Issue 2 C , 2010 , Pages 153-157 ; 10263098 (ISSN) Maghsoodi, V ; Yaghmaei, S ; Sharif University of Technology
    2010
    Abstract
    Production yield of solid-state (SSF) and submerged fermentation (SMF) on chitosan from Aspergillus niger was investigated. A. niger BBRC 20004 was grown on soybean residue and Sabouraud Dextrose Broth medium (2% glucose). Chitosan was extracted from the fungal mycelia using hot alkaline and acid treatment. Soybean residue at a moisture content of 37%, and 8-4 ± 0.26% of nitrogen content produced the highest amount of chitosan, 17.053 ± 0.95 g/kg dry substrate after 12 days. Also, chitosan was extracted from A. niger on Sabouraud Dextrose Broth medium in submerged fermentation (0.8455 g/l after 12 days of cultivation). The yield of chitosan isolated in SSF was about 15-20 times more than in... 

    Simulation of methane gas production process from animal waste in a discontinuous bioreactor

    , Article Biointerface Research in Applied Chemistry ; Volume 11, Issue 6 , 2021 , Pages 13850-13859 ; 20695837 (ISSN) Norouzi, N ; Khajehpour, H ; Sharif University of Technology
    AMG Transcend Association  2021
    Abstract
    Due to the importance of environmental protection and the need to use new energy and alternative to conventional fuels, renewable energy has received much attention. Due to this necessity, a discontinuous bioreactor producing methane gas from animal waste has been modeled and simulated in this research. Monod kinetics was used to express the relationship between the growth rate of microorganisms and substrate concentration. The fourth-order Rong Kuta numerical method solved the substrate consumption and production of microorganisms and methane gas. The effect of the initial concentration of microorganisms on methane production has also been investigated. The initial concentrations of... 

    Optimization of a fed-batch fermenter producing baker's yeast using simulated annealing method

    , Article Iranian Journal of Biotechnology ; Volume 7, Issue 3 , 2009 , Pages 157-165+191 ; 17283043 (ISSN) Ghahremani, H ; Pishvaie, M. R ; Vossoughi, M ; Seyfkordi, A. A ; Sharif University of Technology
    2009
    Abstract
    Modeling of fermentation processes is so complicated and uncertain; therefore it is necessary to provide a robust and appropriate dynamic optimization method. In order to obtain the maximum amount of yeast (Saccharomyces cerevisiae), the bioreactor must be operated under optimal conditions. To determine substrate feeding in a fed-batch bioreactor, a simulated annealing (SA) approach was examined. The optimal glucose feed rate profiles were computed by a stochastic and deterministic problems for various initial conditions to investigate their effects on optimal operation of the fed-batch bioreactor. Results declared a proper capability of SA method for determination of optimal feeding... 

    Modeling and Simulation of Alcoholic Fermentation of Sugarcane Blackstrap Molasses

    , M.Sc. Thesis Sharif University of Technology Soroush, Mohammad (Author) ; Yaghmaee, Sohila (Supervisor)
    Abstract
    Fed-batch fermentation is a valuable and cost-effective method for bio-based production of various products such as ethanol, which has various applications in various industries.In recent years, bioethanol production has been given special attention in many countries. For this reason, the mathematical modeling of production of these products is very important for their optimal and cost-effective production. Given the transient and dynamic nature of fermentation and its specific complexity, mathematical modeling of fed-batch bioreactors is difficult and complicated. In this research, an unstructured model was used to predict the production of ethanol from blackstrap sugar cane molasses based... 

    Production of glucoamylase by aspergillus niger under solid state fermentation

    , Article International Journal of Engineering, Transactions B: Applications ; Volume 25, Issue 1 , 2012 , Pages 1-7 ; 1728-144X (ISSN) Nahid, P ; Vossoughi, M ; Roostaazad, R ; Ahmadi, M ; Zarrabi, A ; Hosseini, S. M ; Sharif University of Technology
    Abstract
    In this study, Glucoamylase production by Aspergillus niger was investigated under solid state fermentation using low cost by-products of agricultural processes as substrate. Highest enzyme production was observed when a combination of wheat bran (WB) and corn flour (CF) was used as compared to WB+ rice bran, WB+ rice flour and WB alone. Several compositions of corn flours were experimented. The best combination of WB in addition of 10% corn flour resulted maximum enzyme activities. Study of the fermentations in flasks revealed 373.3 IU/gds and 41.4 g/l for the enzyme activity and protein concentration respectively under conditions of 30± 1°C, pH 4.7 and time 96 h. Optimum conditions... 

    Solid state fermentation for production of chitosan by aspergillus niger

    , Article International Journal of Engineering, Transactions B: Applications ; Volume 22, Issue 1 , 2009 , Pages 1-6 ; 1728-144X (ISSN) Maghsoodi, V ; Razavi, J ; Yaghmaei, S ; Sharif University of Technology
    Materials and Energy Research Center  2009
    Abstract
    The effect of Solid State Fermentation (SSF) on Chitosan production by A. niger was investigated. A. niger BBRC 20004 from Biochemical and Bioenvironmental Research Centre of Sharif University of Technology (Tehran, Iran), was grown on corn residue. Chitosan was extracted from the fungal mycelia using hot alkaline and acid treatment. A. niger was incubated for 12 days on corn residue with moisture content of 35 % and 1.12 % of nitrogen. The Chitosan was obtained and 10.9 g/kg of Urea dry residue was added in various amounts to the medium in order to evaluate the effect of the nitrogen concentration in the production of Chitosan. The highest amount of Chitosan obtained by 6.5 g of urea after... 

    Production of chitosan by submerged fermentation from Aspergillus niger

    , Article Scientia Iranica ; Volume 16, Issue 2 C , 2009 , Pages 145-148 ; 10263098 (ISSN) Maghsoodi, V ; Razavi, J ; Yaghmaei, S ; Sharif University of Technology
    2009
    Abstract
    The effect of glucose concentration in submerged fermentation (SMF) on chitosan production by Aspergillus niger was investigated. A. niger, BBRC, 20004, from the Biochemical and Bioenvironmental Research Centre at Sharif University of Technology, Tehran, Iran, was grown in a Sabouro Dextrose media. Chitosan was extracted from the fungal mycelia using hot alkaline and acid treatment and after 12 days of cultivation, 0.8455 g chitosan /l of the fermentation medium was obtained. The content of glucose in the Sobouro Dextrose Broth media was also changed and the highest yield of chitosan 0.9121 g/l was obtained in Sobouro Dextrose Broth media containing 8% glucose. © Sharif University of... 

    Continuous solid-state fermentation as affected by substrate flow pattern

    , Article Chemical Engineering Science ; Volume 61, Issue 8 , 2006 , Pages 2675-2687 ; 00092509 (ISSN) Khanahmadi, M ; Mitchell, D. A ; Beheshti, M ; Roostaazad, R ; Sánchez, L. R ; Sharif University of Technology
    2006
    Abstract
    The performance of continuous solid state bioreactors having two different solid substrate flow patterns, namely plug flow and completely mixed flow, is quantified for both steady-state and transient operation using a simple mathematical model. The core assumption is that each substrate particle acts as an infinitesimal bioreactor. The residence time distribution of the particles is considered in the formulation of the equations for the mixed-flow bioreactor and the error that results from neglecting it is investigated by comparing the simulation results with those of a completely mixed, continuous bioreactor for submerged liquid fermentation (a chemostat). The model is extended to include... 

    Optimization of sugarcane bagasse hydrolysis process by economic criteria

    , Article Advances in Environmental Biology ; Volume 5, Issue 7 , 2011 , Pages 1900-1903 ; 19950756 (ISSN) Darouneh, E ; Alavi, A ; Vosoughi, M ; Ardjmand, M ; Seifkordi, A. A ; Zabihi, V ; Radjabi, R ; Hedayat, N ; Sharif University of Technology
    2011
    Abstract
    Various processes are used for production of value-added materials from sugarcane bagasse. Hydrolysis processes are the most commonly used methods for producing new products from this low value byproduct. Sulfuric acid hydrolysis processes are the best processing options due to their fast reaction and low process cost. The goal of this study was to investigate an optimized hydrolysis method which can produce fermentable sugar-containing liquor economically. In the other words it was designed to minimize the toxic materials to a level that cannot affect the citric acid production by Aspergillus niger. Results showed the optimum condition for one-step hydrolysis processes occurs at the... 

    L-sorbose production by gluconobacter oxydans using submerged fermentation in a bench scale fermenter

    , Article Applied Food Biotechnology ; Volume 7, Issue 1 , 2020 , Pages 41-48 Alizad Derakhshi Azar, S ; Alemzadeh, I ; Sharif University of Technology
    National Nutrition and Food Technology Research Institute  2020
    Abstract
    Background and objective: L-Sorbose, as a precursor of ascorbic acid, can be biologically produced using Gluconobacter oxydans. The aim of this study was to optimize production of L-Sorbose by controlling concentration of the substrates and starter cultures. Material and methods: In this study, effects of three various fermentation parameters on the concentration of L-sorbose were assessed using fermenter (28°C, 1.4 vvm) and response surface methodology. These parameters included quantities of D-sorbitol (120-180 g lDw-1) (Deionized water) and yeast extract (6-18 g lDw-1) and inoculum/substrate ratios (5-10%). Results and conclusion: Results showed that the fitted model with high values of... 

    Influence of different nitrogen sources on amount of chitosan production by Aspergillus niger in solid state fermentation

    , Article Iranian Journal of Chemistry and Chemical Engineering ; Volume 27, Issue 1 , 2008 , Pages 47-52 ; 10219986 (ISSN) Maghsoodi, V ; Yaghmaei, S ; Beigi, S. M ; Sharif University of Technology
    2008
    Abstract
    In this study the effect of different nitrogen source substrates on the amount of chitosan production by Aspergillus niger was investigated. A. niger PTCC 5012 from the Persian Type Culture Collection (PTCC) was grown on soy bean, corn seed and canola residues at 30 °C for specified cultivation days under sterilized conditions. Chitosan was extracted from the fungal mycelia using hot alkaline and acid treatment. The results were shown that soy bean residue at moisture of 37% and 8.4 ± 0.26 % of nitrogen content produced the highest amount of chitosan (17.053 ± 0.95 g/kg of dry substrate), after 12 days of incubation. Corn seed residue produced very low amount of chitosan (1.9 ± 0.4 % of... 

    Investigating the use of cooling surfaces in solid-state fermentation tray bioreactors: Modelling and experimentation

    , Article Journal of Chemical Technology and Biotechnology ; Volume 79, Issue 11 , 2004 , Pages 1228-1242 ; 02682575 (ISSN) Khanahmadi, M ; Roostaazad, R ; Safekordi, A ; Bozorgmehri, R ; Mitchell, D. A ; Sharif University of Technology
    2004
    Abstract
    The effect of wall cooling in tray-type solid-state fermenters was investigated by cultivation of Aspergillus niger ATCC 10 864 on wheat bran. Temperature, moisture, pH and glucoamylase activity in the bed were monitored. Application of the heat exchanger plate reduced the overall water loss but increased the heterogeneity of moisture distribution in the bed. Moisture content increased markedly close to the heat transfer plate while the upper regions of the bed dried out. The thermal conductivity of the bed was measured to be 0.19 Wm-1 K-1. At these conditions and depending on the air flow rate, 58-82% of the metabolic heat was removed via conduction towards the plate. A mathematical model...