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JCR 2016
جستجوی مقالات
پنجشنبه 27 آذر 1404
Iranian Journal of Chemical Engineering
، جلد ۲۱، شماره ۳، صفحات ۳۴-۴۸
عنوان فارسی
چکیده فارسی مقاله
کلیدواژههای فارسی مقاله
عنوان انگلیسی
Technical-economic Analysis of Chemical Hydrolysis of Microalgae for Bioethanol Production using SuperPro Designer®
چکیده انگلیسی مقاله
This study simulated the production of bioethanol from mixed microalgae to the assess economic feasibility on an industrial scale. For the first time, the kinetic study of the chemical hydrolysis of mixed microalgae was carried out using the AQUASIM software.
The chemical hydrolysis for the pretreatment of microalgae was carried out using
H
2
SO
4
(2.5%, 5%, 10% (v/v)), H
3
PO
3
(2.5%, 5%, 10% (v/v)), and NaOH (1%, 2%, 4% (v/v))
at the different biomass concentrations (25 to 100 g/L) at the temperature of 121 ℃ for 70 min. Kinetic constants were calculated using experimental data and the AQUASIM software. It was found that the optimum yield of sugars, which was obtained, was about 93%. From the comparison of the values of the
reaction rate constant
(k), it was observed that the hydrolysis rate at 50 g/L by using
H
2
SO
4
2.5% (v/v), is higher compared to 25, 75, and 100 g/L, and the higher
reaction rate constant
supports the faster hydrolysis of algal biomass. These kinetic constants were applied in simulating the process on an industrial scale using the SuperPro Designer software. Experimental and simulation results showed that 3.6 g/L of bioethanol is produced from the 9.3 g/L of glucose under optimal conditions. Also, simulation results using the SuperPro Designer software demonstrated that eliminating the algal biomass drying stage has the potential to save up to 713,000 $ in operational expenses.
کلیدواژههای انگلیسی مقاله
Bioethanol,Microalgae,Chemical hydrolysis,SuperPro Designer,AQUASIM
نویسندگان مقاله
E. Bahmani |
Sahand University of Technology
H. Shokrkar |
Sahand University of Technology
R. Alizadeh |
Sahand University of Technology
نشانی اینترنتی
https://www.ijche.com/article_200616_966bdefd37d80cb55ec8fcf11356001c.pdf
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en
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