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Morteza Khanahmadi

Researcher at Sharif University of Technology

Publications -  26
Citations -  617

Morteza Khanahmadi is an academic researcher from Sharif University of Technology. The author has contributed to research in topics: Solid-state fermentation & Fermentation. The author has an hindex of 12, co-authored 25 publications receiving 469 citations.

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Ethanol production by Mucor indicus and Rhizopus oryzae from rice straw by separate hydrolysis and fermentation

TL;DR: Rice straw was successfully converted to ethanol by separate enzymatic hydrolysis and fermentation by Mucor indicus, Rhizopus oryzae, and Saccharomyces cerevisiae.
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Ethanol production from bread residues

TL;DR: In this paper, bread residues were converted into a suitable fermentation feed via a two-step starch hydrolysis using amylolytic enzymes, which resulted in an overall yield of 350 g ethanol per kg of initial bread dry matter.
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Bioprocessing of agro-industrial residues for optimization of xylanase production by solid- state fermentation in flask and tray bioreactor

TL;DR: This study aimed at optimization of solid-state fermentation by Aspergillus niger CCUG33991 for maximum xylanase production using low-cost agro-industrial residues 1 in tray bioreactor by exploring the effects of particle size, initial moisture content and temperature in trayBioreactor.
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Effect of drought stress on growth parameters, osmolyte contents, antioxidant enzymes and glycyrrhizin synthesis in licorice (Glycyrrhiza glabra L.) grown in the field

TL;DR: In this paper, the effects of mild, moderate and intense drought on growth parameters, osmolyte content, oxidative stress markers, antioxidant enzymes, glycyrrhizin biosynthesis genes, and root glycrhizins concentration and contents, have been assessed in five Iranian licorice genotypes grown in the field.
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Bed moisture estimation by monitoring of air stream temperature rise in packed-bed solid-state fermentation

TL;DR: In this article, the authors developed a method for predicting the moisture content of the fermenting solids in an intermittently mixed packed-bed bioreactor based on measurements of the inlet and outlet gas stream temperatures and the assumption that both the gas streams are saturated with water vapor.