scholarly journals Esterification of Palmitic Acid with Methanol in the Presence of Macroporous Ion Exchange Resin as Catalyst

1970 ◽  
Vol 5 (2) ◽  
Author(s):  
Amelia Qarina Yaakob and Subhash Bhatia
Keyword(s):  
Ion Exchange ◽  
Palmitic Acid ◽  
Exchange Resin ◽  
Batch Reactor ◽  
Simulated Data ◽  
Processing Parameters ◽  
Ion Exchange Resin ◽  
Molar Ratio ◽  
Catalyst Loading ◽  
Amberlyst 15

The esterification of palmitic acid with methanol was studied in a batch reactor using macro porous ion exchange resin Amberlyst 15 as a catalyst. Methyl palmitate was produced from the reaction between palmitic acid and methanol in the presence of catalyst. The effects of processing parameters, molar ratio of alcohol to acid M, (4-10), catalyst loading (0-10 g cat/liter), water inhibition (0-2 mol/liter), agitator speed (200-800 rpm) and reaction temperature (343-373K) were studied. The experimental kinetic data were correlated using homogenous as well as heterogeneous models (based on single as well as dual site mechanisms). The activation energy of the reaction was 11.552 kJ/mol for forward reaction whilst 5.464 kJ/mol for backward reaction. The experimental data fitted well with the simulated data obtained from the kinetic models. Keywords: Palmitic Acid, Methanol, Esterification, Ion Exchange Resin, Kinetics.

scholarly journals Kinetic Study of Catalytic Esterification of Butyric Acid and Ethanol over Amberlyst 15

2013 ◽  
Vol 2013 ◽  
pp. 1-6 ◽  
Author(s):  
Nisha Singh ◽  
Raj kumar ◽  
Pravin Kumar Sachan
Keyword(s):  
Butyric Acid ◽  
Batch Reactor ◽  
Homogeneous Model ◽  
Ion Exchange Resin ◽  
Molar Ratio ◽  
Catalyst Loading ◽  
Esterification Reaction ◽  
Initial Concentration ◽  
Amberlyst 15 ◽  
Variation Of Parameters

The esterification reaction of butyric acid with ethanol has been studied in the presence of ion exchange resin (Amberlyst 15). Ethyl butyrate was obtained as the only product which is used in flavours and fragrances. Industrially speaking, it is also one of the cheapest chemicals, which only adds to its popularity. The influences of certain parameters such as temperature, catalyst loading, initial concentration of acid and alcohols, initial concentration of water, and molar ratio were studied. Conversions were found to increase with an increase in both molar ratio and temperature. The experiments were carried out in a batch reactor in the temperature range of 328.15–348.15 K. Variation of parameters on rate of reaction demonstrated that the reaction was intrinsically controlled. Experiment kinetic data were correlated by using pseudo-homogeneous model. The activation energy for the esterification of butyric acid with ethanol is found to be 30 k J/mol.

scholarly journals Esterification of palmitic acid with epichlorohydrin on anion exchange resin catalyst

2007 ◽  
Vol 5 (3) ◽  
pp. 715-726 ◽  
Author(s):  
Emil Muresan ◽  
Spiridon Oprea ◽  
Theodor Malutan ◽  
Mihai Vata
Keyword(s):  
Palmitic Acid ◽  
Exchange Resin ◽  
Catalyst Particle ◽  
Molar Ratio ◽  
Catalyst Loading ◽  
Esterification Reaction ◽  
Macroporous Resin ◽  
Resin Catalyst ◽  
Catalyst Particle Size ◽  
Rate Of Reaction

AbstractThe esterification reaction of palmitic acid with epichlorohydrin catalyzed by an anionic macroporous resin was studied. Purolite A-500 resin proved to be a very effective catalyst in the synthesis of 3-chloro-2-hydroxypropyl palmitate. The effects of certain parameters such as speed of agitation, catalyst particle size, catalyst loading, temperature, initial molar ratio between reactants on the rate of reaction were studied. It was found that the overall rate is intrinsically kinetically controlled. The structure of synthesized ester was confirmed by FTIR and 1H NMR analyses.

Catalytic Synthesis of Isoamyl Acetate by Ion Exchange Resin-Supported (NH4)6[MnMo9O32] • 8H2O with Waugh Structure

2013 ◽  
Vol 750-752 ◽  
pp. 1231-1234 ◽  
Author(s):  
Li Xia Wang ◽  
Shu Heng Liu ◽  
Hua Yuan ◽  
Lin Lin Guo
Keyword(s):  
Ion Exchange ◽  
Exchange Resin ◽  
Orthogonal Experiment ◽  
Catalytic Efficiency ◽  
Ion Exchange Resin ◽  
Isoamyl Acetate ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
Reaction Conditions ◽  
Optimal Reaction

Ion exchange resin-supported (NH4)6[MnMo9O32]8H2O with Waugh structure is used to prepare supported solid catalyst. Performance of this catalyst is researched by means of synthesis of isoamyl acetate. Optimal reaction conditions determined by orthogonal experiment are as follows: acid-alcohol molar ratio is 2.5:1, reaction time is 120 min, catalyst dosage is 0.8 g, dosage of water-carrying agent is 2.5 ml, esterification yield reaches 95.1%. This catalyst is characterized by high catalytic efficiency, easy separation and recovery, absence of environmental pollution and being reusable, etc.

Activity Comparison of Acidic Resins in the Production of Valuable Glycerol Acetates

2016 ◽  
Vol 14 (1) ◽  
pp. 309-314 ◽  
Author(s):  
Emine Kaya Ekinci ◽  
Gamze Gündüz ◽  
Nuray Oktar
Keyword(s):  
Exchange Resin ◽  
Heterogeneous Reaction ◽  
Reaction System ◽  
Ion Exchange Resin ◽  
Molar Ratio ◽  
Glycerol Conversion ◽  
Amberlyst 15 ◽  
Time Period ◽  
Short Time ◽  
Activity Comparison

AbstractAcetates of glycerol have been produced in a heterogeneous reaction system using acidic ion-exchange resin catalysts; Amberlyst-15 (A-15), Amberlyst-16 (A-16), Amberlyst-36 (A-36), Amberlite-IR 120 (A-IR 120) and Relite-EXC8D (R-EXC8D). Effect of reaction temperature on glycerol conversion and product (mono, di and tri glycerol acetates) selectivities were investigated via reaction experiments conducted with glycerol to acetic acid initial molar ratio (G/Ac) of 1/6. Increase in glycerol conversion with an increase in temperature was observed for all catalysts. Among the catalysts investigated, R-EXC8D exhibited the highest activity in the temperature range of 95–150°C. Reaction was completed within a 25 minute short time period.

Reaction Kinetics of Catalytic Esterification of Nonanoic Acid with Ethanol over Amberlyst 15

2014 ◽  
Vol 12 (1) ◽  
pp. 451-463 ◽  
Author(s):  
Mamta Sharma ◽  
Amrit Pal Toor ◽  
Ravinder Kumar Wanchoo
Keyword(s):  
Batch Reactor ◽  
Cation Exchange Resin ◽  
Initial Reaction Rate ◽  
Molar Ratio ◽  
Catalyst Loading ◽  
Nonanoic Acid ◽  
Initial Reaction ◽  
Exponential Factor ◽  
Amberlyst 15 ◽  
Heterogeneous Esterification

Abstract The kinetic behaviour of heterogeneous esterification of nonanoic acid with ethanol over an acidic cation exchange resin, Amberlyst 15, was investigated in a batch reactor and effect of various parameters such as catalyst loading, molar ratio and reaction temperature on degree of fractional conversion has been studied. Internal and external diffusions were found to be negligible in this study. Nonideality of the liquid phase was taken into account by using activities instead of concentrations. The activity coefficients were estimated using UNIFAC group contribution method. Eley–Rideal (ER) kinetic model was used to interpret the obtained kinetic data. The temperature-dependent initial reaction rate constants and the adsorption coefficients for ethanol and water were determined from the observed experimental data obtained at different initial concentration of acid, alcohol and water. Activation energy and pre-exponential factor of the reaction were found to be 53.7 kJ mol−1 and 1.51×105 l2 g−1 mol−1 h−1 respectively.

Development of pyrolytic monolithic carbon composites for the conditioning of spent ion exchange resins

2012 ◽  
Vol 1475 ◽  
Author(s):  
Pamela B. Ramos ◽  
Néstor O. Fuentes ◽  
Vittorio Luca
Keyword(s):  
Ion Exchange ◽  
Exchange Resin ◽  
Cation Exchange Resin ◽  
Processing Parameters ◽  
Ion Exchange Resin ◽  
Mathematical Functions ◽  
Waste Forms ◽  
Resin Beads ◽  
Temperature Ramp ◽  
Exchange Resins

ABSTRACTThe pyrolysis of ion exchange resin beads that are used for the purification of water in reactor primary- and secondary-cooling circuits can result in stable and leach resistant carbonaceous products. However, free flowing beads are less desirable waste forms for disposal in sub-surface or surface repositories than monolithic masses of low porosity. We have investigated the pyrolysis of polymeric resin – cation exchange resin composites to give mechanically robust and chemically durable monolithic carbonaceous waste forms that are suitable for repository disposition. Also investigated was the dependence of product properties on various processing parameters (temperature ramp and final temperature). As a first approach, epoxy resins were used for the preparation of monoliths since such resins cure at room temperature and result in a relatively high carbon yield. Carbonaceous monolithic products were prepared at 400, 500, 600, 700 and 800 °C using a temperature ramp of 2°C/min. The products were maintained at the chosen temperatures for a period of one hour. Mass losses, volume reduction, hardness and compressive strength were measured and mathematical functions are proposed to describe the measured values of these properties. The carbon monoliths were observed to be mechanically robust.

Carbonylation of formaldehyde over ion exchange resin catalysts. 1. Batch reactor studies

1993 ◽  
Vol 32 (2) ◽  
pp. 253-259 ◽  
Author(s):  
Sang Young Lee ◽  
Jae Chang Kim ◽  
Jae Sung Lee ◽  
Young Gul Kim
Keyword(s):  
Ion Exchange ◽  
Exchange Resin ◽  
Batch Reactor ◽  
Ion Exchange Resin

Hydration of 2-methylbutenes on organic ion exchange resin catalysts

1987 ◽  
Vol 52 (5) ◽  
pp. 1272-1279 ◽  
Author(s):  
Zdeněk Prokop ◽  
Karel Setínek
Keyword(s):  
Ion Exchange ◽  
Reaction Rate ◽  
Exchange Resin ◽  
Ion Exchange Resin ◽  
Exchange Capacity ◽  
Molar Ratio ◽  
Macroporous Resin ◽  
Equilibrium Reaction ◽  
Styrene Divinylbenzene ◽  
Increasing Temperature

The course of the hydration of a mixture of 2-methyl-1-butene and 2-methyl-2-butene in dependence on the structure of strongly acidic styrene-divinylbenzene ion exchange resin catalysts has been studied. The most efficient catalysts turned out to be macroporous ones. The reaction rate increased with increasing temperature, while the amount of the product (2-methyl-2-butanol) in the equilibrium reaction mixture decreased. Similarly, the hydration was strongly affected by the water to alkene molar ratio in the starting reaction mixture. Modification of ion exchange resin catalysts with 1-butylamine did not affect course of the hydration in the case of gel type catalysts, while with macroporous resin catalysts the addition of amine up to 0.5% of the total catalyst exchange capacity showed activating effect.

Preparation of Environment-Friendly Epoxidized Corn Oil as a Plasticizer

2014 ◽  
Vol 852 ◽  
pp. 256-261 ◽  
Author(s):  
Yuan Huai Peng ◽  
Hua Di Lin
Keyword(s):  
Hydrogen Peroxide ◽  
Ion Exchange ◽  
Exchange Resin ◽  
Corn Oil ◽  
Ion Exchange Resin ◽  
Molar Ratio ◽  
Environment Friendly ◽  
Percent Conversion ◽  
Optimized Conditions

An environment-friendly plasticizer, epoxidized corn oil was prepared by the epoxidation of corn oil with peroxyacetic acid which was generated in situ from hydrogen peroxide and glacial acetic using acidic ion exchange resin modified by zinc chloride as catalyst. The product with an epoxy oxygen content of 6.40 w% and a percent conversion to oxirane of 87.67 % was obtained under the following optimized conditions: 15 % modified ion exchange resin feed relative to the weight of corn oil, the molar ratio of 1.7 to 1 with hydrogen peroxide to double bonds, 18% acetic acid feed relative to the weight of corn oil, the reaction time of 5.5 h, the temperature of 75 °C and stirring speed of 600 rpm.

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