Biodiesel Preparation without a Cosolvent in an Opposite-Side Micro-Fixed-Bed Reactor

نویسندگان

چکیده

In the process of preparing biodiesel using microreactors, cosolvents and homogeneous catalysts are generally used, which adds to separation cost. Hence, this study explored use an opposite-side feed micro-fixed-bed reactor with inner diameter 2 mm produce by transesterification soybean oil methanol without any cosolvent, in a fixed solid base acted as catalyst obstacles. A yield 99.4% was achieved when methanol-to-oil molar ratio 12, temperature 70 °C, residence time 8.05 min. mixing conducted for microreactor through computational fluid dynamics (CFD) simulations. The results showed that best index could reach 0.94 within 25 (length). Then, kinetics were found be consistent proposed pseudo-homogeneous secondary reaction model. With data mixed-model, predicted. simulated experimental data.

برای دانلود باید عضویت طلایی داشته باشید

برای دانلود متن کامل این مقاله و بیش از 32 میلیون مقاله دیگر ابتدا ثبت نام کنید

اگر عضو سایت هستید لطفا وارد حساب کاربری خود شوید

منابع مشابه

V2O5-MoO3 Catalysts Preparation and Performance Testing on the Oxidation of Benzene to Maleic Anhydride in a Fixed Bed Reactor

In this research, the selective oxidation of benzene to maleic anhydride (MAN) in a fixed-bed reactor was studied. The gas phase catalytic oxidation of benzene was carried outin a laboratory scale fixed bed reactor on the catalysts, which were prepared having two different compositions on silica gel. The effects of temperature, flow rates of benzene and air, and catalyst type on the reactio...

متن کامل

Using Continuous Integrated Micro Filtration for the Production of Pseudotype Vectors in a Fixed Bed Reactor

Retroviral pseudotype vector, derived from the murine leukaemia virus carrying the HIV-1 envelop protein MLV (HIV-1) were produced using a integrated, continuous cultivation and harvest process. A 200ml fix bed reactor was used to cultivate the anchorage dependent packaging cell line on macro-porous carriers until the maximum glucose uptake was reached. After starting the cultivation in batch m...

متن کامل

CFD Simulation of Dimethyl Ether Synthesis from Methanol in an Adiabatic Fixed-bed Reactor

A computational fluid dynamic (CFD) study of methanol (MeOH) to dimethyl ether (DME) process in an adiabatic fixed-bed reactor is presented. One of the methods of industrial DME production is the catalytic dehydration of MeOH. Kinetic model was derived based on Bercic rate. The parameters of this equation for a specific catalyst were tuned by solving a one-dimensional homogenous model using MAT...

متن کامل

Modeling Wood Gasification in a Countercurrent Fixed-Bed Reactor

A one-dimensional, unsteady mathematical model is presented of fixed-bed countercurrent wood gasifiers, which couples heat and mass transport with wood drying and devolatilization, char gasification, and combustion of both char and gas-phase species. The model is used to simulate the structure of the reaction fronts and the gasification behavior of a laboratory-scale plant as the reactor throug...

متن کامل

Determination of the Product Selectivity Model from the Fischer Tropsch Synthesis in a Fixed Bed Reactor

The Fischer-Tropsch synthesis is a catalytic process that can produce a fuel similar to fossil fuels by using primary sources such as agricultural waste and carbon sources that can convert into synthesis gas by superheated steam. All fuel derivatives can be supplied through the Fischer-Tropsch reaction. The synthesis produces a variety of hydrocarbons via parallel and sequential reactions. Howe...

متن کامل

ذخیره در منابع من


  با ذخیره ی این منبع در منابع من، دسترسی به آن را برای استفاده های بعدی آسان تر کنید

ژورنال

عنوان ژورنال: Energies

سال: 2023

ISSN: ['1996-1073']

DOI: https://doi.org/10.3390/en16124798