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.

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.

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

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.

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%.

Catalytic Synthesis of N-Butyl Acetate by Silicotungstic Acid Supported on Bentonite

2012 ◽  
Vol 550-553 ◽  
pp. 362-365
Author(s):  
Jian Zhong Jin
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Reaction Temperature ◽  
Butyl Acetate ◽  
Molar Ratio ◽  
Main Reaction ◽  
Incipient Wetness Impregnation ◽  
Impregnation Method ◽  
Silicotungstic Acid ◽  
Acid Loading

A series of solid acid catalysts were synthesized by incipient wetness impregnation method by varying the wt% of silicotungstic acid on bentonite. Silicotungstic acid supported on bentonite was used to catalytic synthesise of n-butyl acetate with acetic acid and n-butyl alcohol . The main reaction parameters such as silicotungstic acid loading on bentonite, the amount of catalyst, molar ratio of reactants, reaction temperature and reaction time have been investigated. The optimum conditions were determined as follows : silicotungstic acid loading on bentonite 20 wt %, catalyst 0.7 g , mole ratio of n-butanol to acetic acid 1:1.1, reaction temperature 98 °C and reaction time 2 h . The esterification yield of n-butyl acetate was about 98.2 %. The catalyst could be used repeatedly for many times without distinct loss in activity.

Study on the Influence of Different Catalysts on the Preparation of Ethyl Levulinate from Biomass Liquefaction

2020 ◽  
Vol 14 (3) ◽  
pp. 396-400
Author(s):  
Shuhua Yang ◽  
Qian Guan ◽  
Zijie Li ◽  
Haiyan Xu ◽  
Zhiwei Wang ◽  
...  
Keyword(s):  
Sulfuric Acid ◽  
Reaction Time ◽  
Reaction Temperature ◽  
Raw Materials ◽  
Raw Material ◽  
Reaction Conditions ◽  
Ethyl Levulinate ◽  
Catalyst Type ◽  
Optimum Reaction ◽  
Catalyst Dosage

The liquefaction experiments of straw biomass under heating and pressure were carried out with sulfuric acid and three ionic liquids as catalysts, 1-Butyl-3-methylimidazolium chloride ([BMIM] [Cl]), 1-Butyl-3-methylimidazolium hydrogen sulfate ([BMIM] [HSO4]), 1-methyl-3-(4-sulfobutyl) imidazole bisulphate ([HSO3-BMIM] [HSO4]), and anhydrous ethanol as solvent. The effects of catalyst type and dosage, reaction time and reaction temperature on liquefaction were investigated and optimized. The results showed that under the catalysis of sulfuric acid, the yield of ethyl levulinate was the highest; [HSO3-BMIM] [HSO4], the conversion of raw materials was the highest; when sulfuric acid was used as catalyst, the optimum reaction conditions were catalyst dosage 10%, reaction temperature 190 °C, reaction time 60 min, the yield of ethyl levulinate (EL) was 18.11%, and the conversion of raw materials was 75%. When [HSO3-BMIM] [HSO4] was used as catalyst, the optimum reaction conditions were as follows: catalyst dosage 26%, reaction temperature 200 °C, reaction time 60 min, the yield of EL was 10.2%, conversion of raw material 85.31%.

Study on Pre-Esterification of Trench Oil and Preparation of Bio-Diesel

2013 ◽  
Vol 724-725 ◽  
pp. 1054-1061
Author(s):  
Zhi Hong Xiao ◽  
Ai Hua Zhang ◽  
Wei Wei Jiang ◽  
Hong Qin Zhang ◽  
Chang Zhu Li
Keyword(s):  
Ionic Liquid ◽  
Ionic Liquids ◽  
Reaction Time ◽  
Reaction Temperature ◽  
Raw Materials ◽  
Acid Methyl Ester ◽  
Molar Ratio ◽  
Acid Methyl ◽  
Basic Ionic Liquid

In this study, the trench oil was processed by the technology of polyol pre-esterification and the bio-diesel was prepared using basic ionic liquid 1-methyl-3-butyl-imidazole hydroxide as a catalyst. The amount of ionic liquids, alcohol and oil molar ratio, reaction temperature and reaction time were investigated on the transesterification reaction. The results showed that the bio-diesel prepared conditions by trench oil are as follows: alcohol and oil molar ratio of 8:1, reaction temperature 70°C, reaction time 110min and the amount of catalyst for the quality of raw materials 3.0% oil. Under these conditions, fatty acid methyl ester was 95.7% conversion rate.

Study on the Synthesis of Isoamyl Acetate Catalyzed by Strong Acidic Cation Exchange Resin

2011 ◽  
Vol 396-398 ◽  
pp. 2411-2415 ◽  
Author(s):  
Ping Lan ◽  
Li Hong Lan ◽  
Tao Xie ◽  
An Ping Liao
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Cation Exchanger ◽  
Cation Exchange Resin ◽  
Isoamyl Acetate ◽  
Molar Ratio ◽  
Esterification Reaction ◽  
Reaction Conditions ◽  
Optimum Reaction

Isoamyl acetate was synthesized from isoamylol and glacial acetic acid with strong acidic cation exchanger as catalyst. The effects of reaction conditions such as acid-alcohol ratio, reaction time, catalyst dosage to esterification reaction have been investigated and the optimum reaction conditions can be concluded as: the molar ratio of acetic acid to isoamylol 0.8:1, reaction time 2h, 25 % of catalyst (quality of acetic acid as benchmark). The conversion rate can reach up to 75.46%. The catalytic ability didn’t reduce significantly after reusing 10 times and the results showed that the catalyst exhibited preferably catalytic activity and reusability.

The role of acidity profile in the nanotubular growth of polyaniline

2010 ◽  
Vol 64 (1) ◽  
Author(s):  
Elena Konyushenko ◽  
Miroslava Trchová ◽  
Jaroslav Stejskal ◽  
Irina Sapurina
Keyword(s):  
Acetic Acid ◽  
Sulfuric Acid ◽  
Reaction Temperature ◽  
Subsequent Growth ◽  
Subsequent Oxidation ◽  
Ammonium Peroxydisulfate ◽  
Aniline Oligomers ◽  
Positive Effect ◽  
Granular Morphology

AbstractConditions of polyaniline (PANI) nanotubes preparation were analyzed. Aniline was oxidized with ammonium peroxydisulfate in 0.4 M acetic acid. There are two subsequent oxidation steps and the products were collected after each of them. At pH > 3, neutral aniline molecules are oxidized to non-conducting aniline oligomers. These produce templates for the subsequent growth of PANI nanotubes, which takes place preferably at pH 2–3. At pH < 2, granular morphology of the conducting PANI is obtained. High final acidity of the medium should be avoided in the preparation of nanotubes, e.g., by reducing the amount of sulfuric acid which is a by-product. Reduction of the peroxydisulfate-to-aniline mole ratio was tested for this purpose in the present study. Lowering of the reaction temperature from 20°C to −4°C had a positive effect on the formation of nanotubes.

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