scholarly journals Esterification of glycerol with acetic acid over Lewatit catalyst

2018 ◽  
Vol 154 ◽  
pp. 01028 ◽  
Author(s):  
Lucky Setyaningsih ◽  
Fahmi Siddiq ◽  
Aqila Pramezy
Keyword(s):  
Acetic Acid ◽  
Optimum Condition ◽  
Reaction Temperature ◽  
Raw Materials ◽  
Environmentally Friendly ◽  
Liquid Fuels ◽  
Molar Ratio ◽  
Derivative Products ◽  
Glycerol Esterification ◽  
Glycerol Derivative

Tri Acetyl Glycerol or triacetin is one of the glycerol derivative products which can be used as additives in liquid fuels (octane boosters) to reduce knocking on the machine. The use of triacetin as octane booster is considered very promising because it comes from renewable and environmentally friendly raw materials. The resulting glycerol-based additives are suitable for gasoline, biodiesel and diesel. In this study glycerol esterification with acetic acid over Lewatit catalyst was investigated. The effects of various parameters, such as reaction temperature, weight of catalyst and molar ratio of glycerol to acetic acid were studied and the optimum condition for the triacetin synthesis are 100°C, 1: 7 mole of ratio and 3% weight of catalys

Synthesis of Fragrance 1-(3,3-dimethylcyclohexyl)Ethyl Acetate

2013 ◽  
Vol 781-784 ◽  
pp. 983-987
Author(s):  
De Li Shen ◽  
Xin He ◽  
Wei Guan ◽  
Yu Ping Liu ◽  
Bao Guo Sun
Keyword(s):  
Acetic Acid ◽  
Sulfuric Acid ◽  
Reaction Time ◽  
Ethyl Acetate ◽  
Reaction Temperature ◽  
Raw Materials ◽  
Molar Ratio ◽  
Gas Chromatography Mass Spectrometry ◽  
Floral Odor ◽  
Odor Evaluation

1-(3,3-dimethylcyclohexyl) ethyl acetate was synthesized by the reaction of dihydromycene with acetic acid in the presence of sulfuric acid. The effecting factors including the amount of catalyst, the reaction temperature, the molar ratio of raw materials and the reaction time were investigated. The experimental results showed that the molar raio of the dihydromyrcene to acetic acid to sulfuric acid was 1:3:0.2, the reaction temperature is 60 °C and the reaction time was 6.5 h. The yield reached 45.3%. The structure of product was characterized by gas chromatography, mass spectrometry, infrared spectroscopy and nuclear magnetic resonance. The odor evaluation result indicated that the product had a sweet, woody, floral odor.

Synthetic Technology and Performance of a Novel Fatty Alcohol Polyoxyethylene Carboxylate Surfactants

2011 ◽  
Vol 298 ◽  
pp. 163-168 ◽  
Author(s):  
Yuan Yuan Lei ◽  
Guo Zheng ◽  
Yu Sun ◽  
Yong Zhou
Keyword(s):  
Reaction Time ◽  
Optimum Condition ◽  
Sodium Hydroxide ◽  
Fatty Alcohol ◽  
Succinic Anhydride ◽  
Foam Stability ◽  
Raw Materials ◽  
Molar Ratio ◽  
New Type ◽  
And Performance

In this paper, with fatty alcohol polyoxyethylene (AEO9), succinic anhydride (SA) and sodium hydroxide as raw materials, a new type of fatty alcohol polyoxyethylene carboxylate surfactants (SAE9C-Na) was obtained by esterification and neutralizing effect. The influencing factors were researched and its surface properties were studied. The optimum condition of synthesis was determined: molar ratio of alcohol to acid was 1:1.1, reaction temperature was 85°C, reaction time was 60 min, under this condition, the yield could reach up to 95.8%. The results received from this experiment showed that SAE9C-Na had excellent surface activity and foaming and foam stability, whose emulsification and solubility enhancement were improved greatly.

Thermodynamic Analysis of Chemical Vapor Deposition Progress for SiC Coatings

2014 ◽  
Vol 633 ◽  
pp. 183-188 ◽  
Author(s):  
Ming Wei Chen ◽  
Hai Peng Qiu ◽  
Jian Jiao ◽  
Xiu Qian Li ◽  
Yu Wang ◽  
...  
Keyword(s):  
Chemical Vapor Deposition ◽  
Thermodynamic Analysis ◽  
Reaction Temperature ◽  
Vapor Deposition ◽  
Raw Materials ◽  
Chemical Vapor ◽  
Molar Ratio ◽  
System Pressure ◽  
Optimal Reaction Temperature ◽  
Sic Coatings

Equilibrium compositions of chemical vapor deposition progress for silicon carbide (CVD-SiC) coatings with MTS/H2 mixture system were calculated by means of HSC Chemistry5.0 code, and influences of the reaction temperature (T), the system pressure (P) and the composition of raw materials (molar ratio of H2 to SiCH3Cl3, β) were investigated. Thermodynamic analysis showed that the value of nC /nSiC in reaction product decreased to a minimum and then increased with the increase of the reaction temperature between 700-1600°C, which meant an optimal reaction temperature existed theoretically for CVD-SiC coatings with highest purity. Furthermore, CVD-SiC coatings with high purity were obtained by experiments under the reaction pressure of 10kPa, H2/SiCH3Cl3 value of 10 and reacton temperature of 1100°C, which was in accordance with the theoretical prediction.

Catalytic Synthesis of Ethyl Acetate Using Ti2SnC

2013 ◽  
Vol 634-638 ◽  
pp. 628-631
Author(s):  
Yun Hui Long ◽  
Jun Ming Guo ◽  
Du Shu Huang ◽  
Gui Yang Liu
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Ethyl Acetate ◽  
Reaction Temperature ◽  
Conversion Rate ◽  
Reaction System ◽  
Catalytic Performance ◽  
Catalytic Synthesis ◽  
Molar Ratio ◽  
The Ideal

The catalytic synthesis of ethyl acetate from ethanol and acetic acid using Ti2SnC in liquid phase under the atmospheric pressure was studied. The influences of some factors such as catalyst usage, initial reactant molar ratio, reaction temperature and reaction time on acetic acid conversion rate of this reaction system were investigated. The acetic acid conversion rate of 88.12% is achieved while the molar ratio of alcohol and acid is 1:3.6, the amount of catalyst is 0.2000 g, the reaction temperature is 80 °C and the reaction time is 30min. The catalyst Ti2SnC is the ideal catalyst for synthesis of ethyl acetate for good catalytic performance, non-corrosive to equipment, easily separated from product and used repeatedly.

Exploration of Chemical Oxidation of p-Cymene

2011 ◽  
Vol 396-398 ◽  
pp. 1132-1137
Author(s):  
Liang Wu Bi ◽  
Qiu Ge Zhang ◽  
Zhen Dong Zhao ◽  
Da Wei Li
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Benzoic Acid ◽  
Sulphuric Acid ◽  
Potassium Permanganate ◽  
Reaction Temperature ◽  
Chemical Oxidation ◽  
Molar Ratio ◽  
Acid Reaction ◽  
By Products

The chemical oxidation of p-cymene was preliminarily studied by several oxidants. The conversion of p-cymene and selectivity of p-cymen-8-ol were both influenced by the factors such as dosage of oxidant, dosage of sulphuric acid, reaction time, reaction temperature and solvent variety. The reasonable oxidation conditions were molar ratio of p-cymene to potassium permanganate 1:3, molar ratio of sulphuric acid to potassium permanganate 0.13:1, mixture of water and acetic acid (1:1, v/v) as solvent, reaction temperature 80 °C and reaction time 9 h. The conversion of p-cymene and selectivity of p-cymen-8-ol were respectively 92.21 % and 69.65 % in the reasonable oxidation conditions. The by-products of p-cymene oxidation mainly included p-iso-propyl benzoic acid, p-isopropyl benzaldehyde and p-methyl acetophenone.

Esterification of glycerol with acetic acid using a sulfonated polyphenylene sulfide non-woven fabric as a catalyst

2020 ◽  
Vol 18 (12) ◽  
Author(s):  
Xueyang Li ◽  
Jiao Zhang ◽  
Yunfei Song ◽  
Yanhong Ji ◽  
Mohammad Younas ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Reaction Temperature ◽  
Polyphenylene Sulfide ◽  
Woven Fabric ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
Glycerol Conversion ◽  
Good Catalytic Activity ◽  
Reaction Cycles

AbstractIn this work, the esterification of glycerol with acetic acid (HOAc) was investigated under sulfonated polyphenylene sulfide non-woven fabric (SPSF) as a solid catalyst. The effects of the amount of catalyst, reaction temperature, molar ratio of glycerol to HOAc and the reaction time on the esterification were studied in detail. It was found that SPSF has good catalytic activity and stability. Under the reaction conditions of the molar ratio of glycerol/HOAc of 1:6 (glycerol 0.1 mol), the reaction temperature of 110 °C, the amount of catalyst of 3 g, and the reaction time of 2 h, the glycerol conversion and the selectivity to diacetin (DAG) reached upto 96 and 56.1%, respectively. Reusability test of SPSF showed that no significant declination in the glycerol conversion and the selectivity was observed after five reaction cycles. The experimental results proved the esterification of glycerol with HOAc by SPSF a promising and green process.

A Kinetic Study of Glycerol Esterification with Acetic Acid Over a Commercial Amberlyst-35 Ion Exchange Resin

2019 ◽  
Vol 70 (7) ◽  
pp. 2325-2329
Author(s):  
Ionut Banu ◽  
Grigore Bozga ◽  
Gheorghe Bumbac ◽  
Alin Vintila ◽  
Sanda Velea ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Exchange Resin ◽  
Ion Exchange Resin ◽  
Molar Ratio ◽  
Glycerol Conversion ◽  
Molar Ratios ◽  
Simple Kinetic Model ◽  
Petroleum Derivatives ◽  
Glycerol Esterification ◽  
Autoclave Reactor

The increased quantities of glycerol available on the market initiated research efforts oriented to new valorization technologies, particularly by its conversion into medium tonnage chemicals, replacing petroleum derivatives. In this work it was investigated the valorization of glycerol by its transformation in glycerol acetates, by direct esterification with acetic acid, over a commercial Amberlyst-35 resin. Experiments were carried out batch-wise, in an autoclave reactor under controlled working conditions, at temperatures between 95 and 112 oC and initial acetic acid to glycerol molar ratios between 4 and 9. The experimental data evidenced that the glycerol conversion to monoacetate is faster than the next esterification steps. A relatively simple kinetic model was proposed and its parameters were evaluated from the experimental measurements. It proved reasonable predicting capacity for products distribution dependencies on the reactants molar ratio and reaction temperature.

scholarly journals Preparation of Biodiesel through Transesterification of Animal Oil and AlcoholUnder the Catalysis of SO42-/ TiO2

2009 ◽  
Vol 6 (1) ◽  
pp. 189-195 ◽  
Author(s):  
Xiu-Yan Pang ◽  
Ting-Ting You
Keyword(s):  
Reaction Time ◽  
Optimum Condition ◽  
Reaction Temperature ◽  
Raw Materials ◽  
Orthogonal Experiment ◽  
Hydrolysis Product ◽  
Mass Ratio ◽  
Optimum Conditions ◽  
Activation Temperature ◽  
Effective Catalyst

Biodiesel was obtained through transesterification of animal oil and ethanol under the catalysis of SO42-/ TiO2We have inspected the activation of SO42-/ TiO2prepared under different dipping vitriol concentration，baking activation temperature. The optimum conditions to prepare SO42-/ TiO2are; dipping vitriol concentration of TiCl4 hydrolysis product is 1.5 mol / L, baking activation temperature for this catalyst takes 500°C. It can guarantee the catalyst has a smaller size and a higher load of vitriol. With animal oil as raw materials, ethanol as transesterifying agent and SO42-/ TiO2as catalyst, the influence of reaction time, mass ratio of ethanol to oil and the dosage of catalyst were investigated. Optimum condition to obtain biodiesel was studied through orthogonal experiment, and it is listed as follow: mass ratio of ethanol to oil is 1.5:1.0, dosage of catalyst is 30 g SO42-/ TiO2versusper 100 g animal oil, and reaction time is 8.0 h when reaction temperature is controlled as 80°C. The yield of biodiesel is 0.796 g/g under the above condition. SO42-/ TiO2can be used as an effective catalyst during transesterification of animal oil and ethanol, and it can be reused

Synthesis of Benzaldehyde 1, 2-Propanediol Acetal by Using Ionic Liquid [Hmim]HSO4 as Catalyst

2012 ◽  
Vol 550-553 ◽  
pp. 400-403 ◽  
Author(s):  
Xue Nan Sun ◽  
Li Cui ◽  
Tong Kuan Xu ◽  
Da Zhi Wang
Keyword(s):  
Ionic Liquid ◽  
Reaction Time ◽  
Reaction Temperature ◽  
Raw Materials ◽  
Product Yield ◽  
Experimental Results ◽  
Molar Ratio ◽  
Reaction Conditions ◽  
Good Catalyst ◽  
Optimal Reaction

Benzaldehyde 1, 2-propanediol acetal was synthesized from benzaldehyde and 1, 2-propanediol in the presence of ionic liquid [HMIM]HSO4. The effect of the amount of catalyst, reaction time, reaction temperature, and the molar ratio of raw materials agent on the product yield was investigated respectively. Experimental results demonstrate that ionic liquid [HMIM]HSO4is a good catalyst for preparation of benzaldehyde 1, 2-propanediol acetal. Results showed the optimal reaction conditions are as follows: the mole ratio of benzaldehyde to 1, 2-propanediol is 1：1.3, the amount of catalyst is 3.0g, the reaction temperature is 343K, and the reaction time is 4h. The achieved yield of acetal is 78. 7%.

Preparation of Cryolite from Industrial Grade Sodium Fluorosilicate

2013 ◽  
Vol 668 ◽  
pp. 149-152
Author(s):  
Rui Ran Liu ◽  
Yun Ren Qiu
Keyword(s):  
Reaction Temperature ◽  
Raw Materials ◽  
Phosphate Fertilizer ◽  
First Grade ◽  
Quality Standard ◽  
Decomposition Temperature ◽  
Molar Ratio ◽  
Novel Technology ◽  
Industrial Grade ◽  
Production Effects

A novel technology of preparing cryolite free of wastewater containing ammonia was studied by using industrial grade sodium fluorosilicate from phosphate fertilizer production. Effects of reaction temperature and pH were studied for the decomposition of sodium fluorosilicate, and the suitable reaction conditions were decomposition temperature above 54 °C and pH 8.4. Effects of Na/Al (molar ratio of Na to Al in the raw materials), reaction temperature and pH on the quality of cryolite were investigated for the synthesis of cryolite. The results indicate that the obtained cryolite can meet the national first-grade quality standard of China at the conditions of pH from 3.0 to 5.0, Na/Al from 2.8 to 3.0 and temperature above 70 °C.

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