Catalytic Synthesis of Isoamyl Acetate Catalyzed by (NH4)6[MnMo9O32]•8H2O Supported Activated Carbon with Waugh Structure

2013 ◽  
Vol 781-784 ◽  
pp. 190-193
Author(s):  
Mei Xu ◽  
Hua Yuan ◽  
Wei Liu ◽  
Jian Wang ◽  
Feng Zhen Yang
Keyword(s):  
Acetic Acid ◽  
Activated Carbon ◽  
Reaction Time ◽  
Conversion Rate ◽  
Isoamyl Alcohol ◽  
Isoamyl Acetate ◽  
Catalytic Synthesis ◽  
Molar Ratio ◽  
Reaction Conditions ◽  
Optimum Reaction

The synthesis of isoamyl acetate with ammonium 9-molybdate manganese heteropolyacid salt supported activated carbon as catalyst was studied. The optimum reaction conditions are obtained as follows: isoamyl alcohol to acetic acid molar ratio = 1.646, the weight of catalyst is 40% of total weigh, m (acidulate catalyst)=0.2g, m (water carrying reagent toluene) = 3ml, reaction time is about 63 minutes. Selectivity is 100% and conversion rate is 89.48%.

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.

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 Estrification of Acetic Acid with Isoamyl Alcohol over Expandable Graphite Catalyst

2008 ◽  
Vol 5 (1) ◽  
pp. 149-154 ◽  
Author(s):  
Xiu-Yan Pang ◽  
Pu Lv ◽  
Yi-Shuang Yang ◽  
Hai-Li Ren ◽  
Fei Gong
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Orthogonal Experiment ◽  
Isoamyl Alcohol ◽  
Isoamyl Acetate ◽  
Esterification Reaction ◽  
Expandable Graphite ◽  
Diffraction Spectrum ◽  
X Ray Diffraction ◽  
Reaction Conditions

The catalysis of expandable graphite for esterification of acetic acid with isoamyl alcohol has been studied. Expandable graphite was prepared with three different methods. In esterification reaction, the influences of catalyst amount, materials ratio, reaction time, prepared method of the expandable graphite on esterification reaction were discussed. X-ray diffraction spectrum of expandable graphite testified the existence of H2SO4intercalation reaction. Through L9(34) orthogonal experiment, optimum esterification reaction conditions were gained as: n(isoamyl alcohol):n(acetic acid)=1.5:1, w(catalyst with a expandable volume of 290 mL•g-1) = 7.5% total amount of materials, reaction time 1.5 h, and temperature keeping at the boiling point. Yield of isoamyl acetate reachs 96.0%. It was testified that expandable graphite was a kind of effective catalyst in the esterification of acetic acid with isoamyl alcohol.

Catalytic Synthesis of Benzyl Acetate by Diatomite Supported Waugh-Type (NH4)6[MnMo9O32] •8H2O

2013 ◽  
Vol 483 ◽  
pp. 38-41
Author(s):  
Shu Heng Liu
Keyword(s):  
Acetic Acid ◽  
Catalytic Activity ◽  
Reaction Time ◽  
Catalytic Synthesis ◽  
Orthogonal Test ◽  
Solid Catalyst ◽  
High Catalytic Activity ◽  
Benzyl Acetate ◽  
Reaction Conditions ◽  
Catalyst Dosage

Take Waugh-Type (NH4)6[MnMo9O32] •8H2O absorbed on diatomite and prepared supported solid catalyst. The properties of the catalyst were studied through the synthesis of benzyl acetate. The appropriate reaction conditions were obtained by orthogonal test: mole ratio of acetic acid to benzyl alcohol was 2.5:1.0, the catalyst dosage was 1.6g, the water carrying agent toluene dosage was 2.5ml, reaction time was 150min, esterification yield was 87.4%. The catalyst are high catalytic activity and non- polluting, and could be reused.

Optimization of Methyl Ester Production from Waste Palm Oil Using Activated Carbon Supported Calcium Oxide Catalyst

2018 ◽  
Vol 280 ◽  
pp. 346-352
Author(s):  
Zuraida Wan ◽  
Bassim H. Hameed ◽  
N. Mohammad Nor ◽  
Nur Alwani Ali Bashah
Keyword(s):  
Activated Carbon ◽  
Reaction Time ◽  
Methyl Ester ◽  
Calcium Oxide ◽  
Palm Oil ◽  
Molar Ratio ◽  
Solid Base ◽  
Catalyst Amount ◽  
Optimum Reaction ◽  
Waste Cooking Palm Oil

In this study, methyl ester (ME) was produced by transesterification of waste cooking palm oil (WPO) using activated carbon supported calcium oxide as a solid base catalyst (CaO/AC). Process optimization using response surface methodology (RSM) was applied to study the effect of reaction time, molar ratio of methanol to oil, reaction temperature and catalyst amount to produce highest ME content. The optimum reaction condition was at 5.5 wt% catalyst amount, 170 °C temperature, 15:1 methanol to oil molar ratio and 2 h 22 min reaction time. The predicted and experimental ME content were found to be 80.02% and 77.32%, respectively.

Catalytic Oxidation of o-chlorotoluene to o-chlorobenzaldehyde by Vanadium Doped Anatase Mesoporous TiO2

2013 ◽  
Vol 781-784 ◽  
pp. 182-185 ◽  
Author(s):  
Sheng Chun Yang ◽  
Jia Qiang Wang
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Catalytic Oxidation ◽  
Reaction Temperature ◽  
Catalytic Reaction ◽  
Conversion Rate ◽  
Reaction Conditions ◽  
Novel Method

A novel method for the catalytic oxidation of o-chlorotoluene (OCT) to o-chlorobenzaldehyde (CBD) was proposed using vanadium doped anatase mesoporous TiO2 (V/MTiO2), the catalytic reaction conditions were investigated. Under the optimum catalytic reaction conditions: 10 mL of acetic acid 100 °C of reaction temperature, 10 h of reaction time and 100 mg of catalyst, the conversion rate of OCT could reach to 95.3%, with a selectivity of 63.5%.

Synthesis of Biodiesel by Phase Transfer Catalysis

2013 ◽  
Vol 291-294 ◽  
pp. 355-358 ◽  
Author(s):  
Yan Qin Huang
Keyword(s):  
Reaction Time ◽  
Soybean Oil ◽  
Reaction Temperature ◽  
Phase Transfer Catalysis ◽  
Phase Transfer ◽  
Molar Ratio ◽  
Mass Ratio ◽  
Reaction Conditions ◽  
Optimum Reaction

Biodiesel was synthesized starting soybean oil and methanol using K2CO3 and phase-transfer catalysis TBAB. It was studied that the yield of biodiesel can be changed with reaction factors such as the kind and the amount of phase-transfer catalysis, the amount of K2CO3, reaction time, molar ratio between methanol and soybean oil, reaction temperature. The results show that the reaction conditions are as following: mass ratio of TBAB to soybean oil weight 0.6%, mass ratio of K2CO3 to soybean oil weight 1.5%, molar ratio between methanol and soybean oil 6∶1, reaction time 20 min, reaction temperature 40 °C. The yield of biodiesel reached 95% under the optimum reaction conditions.

Transesterification of NDC with EG: Effects of Reaction Conditions on NDC Conversion

2013 ◽  
Vol 807-809 ◽  
pp. 2774-2778
Author(s):  
Lin Ping Sun ◽  
Qian Qiao
Keyword(s):  
Reaction Time ◽  
Ethylene Glycol ◽  
Reaction Temperature ◽  
Zinc Acetate ◽  
Metal Salt ◽  
Metal Salts ◽  
Molar Ratio ◽  
Temperature Reaction ◽  
Reaction Conditions ◽  
Optimum Reaction

Transesterification of dimethyl 2,6-napthalene dicarboxylate with ethylene glycol over metal salts catalyst was empolyed as probe reation. The effects of reaction temperature, reaction time, the molar ratio of ethylene glycol to dimethyl 2,6-napthalene dicarboxylate, N2 flowrate, kind of metal salt on the conversion of dimethyl 2,6-napthalene dicarboxylate have been investigated. The results showed that the sequence of influence was as follows: reaction temperature > reaction time > ethylene glycol/dimethyl 2,6-napthalene dicarboxylate molar ratio > amount of the catalyst. The optimum reaction conditions were 210 oC of reaction temperature, 240 min of reaction time, 2.8 molar ratio of ethylene glycol to dimethyl 2,6-napthalene dicarboxylate, 60 ml/min of N2, amount of zinc acetate being 0.08 % / mole of dimethyl 2,6-napthalene dicarboxylate.

scholarly journals Esterification of acetic acid with alcohol isoamyl in the presence of enzymatic catalyst

2019 ◽  
Vol 19 (2) ◽  
pp. 225-242
Author(s):  
Nádia Ligianara Nyari ◽  
Alessandro Rogerio Paulazzi ◽  
Raquel Vera Zamadei ◽  
Jamile Zeni ◽  
Rogério Marcos Dallago
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Food Industry ◽  
Immobilized Lipase ◽  
Isoamyl Alcohol ◽  
Isoamyl Acetate ◽  
Ester Synthesis ◽  
Immobilized Catalyst ◽  
Ultrasound System ◽  
Enzymatic Catalyst

The Candida antarctica Lipase B immobilized on polyurethane catalysed esterification of acetic acid with isoamyl alcohol in mechanical and ultrasonic system in a system solvent-free, was studied. The maximum esterification of isoamyl acetate used immobilized catalyst was the highest esterification, 666.05 U/g with 19 cycles of reuse after 360 minutes of reaction time in mechanical system and 1319.48 U/g was observed and 14 cycles de reuse after 60 minutes of reaction time in ultrasound system. Thus, the process was considered efficient with significant reduction of the reaction time, low instrumental requirements and improve the bioprocess performance. Until now, there were no studies available in the open literature in relation to the ester synthesis catalyzed by immobilized Lipase in polyurethane as support in the ultrasound system. In addition, considered an environmentally correct and economically viable technology, it can be used in cosmetics, pharmaceuticals and food industry.

Selective Epoxidation of Styrene with Mn-TAML/TBHP

2014 ◽  
Vol 685 ◽  
pp. 133-136 ◽  
Author(s):  
Ge Wang ◽  
Ran Li ◽  
Ya Ru Liu ◽  
Hui Ying Liu ◽  
Zhi Min Sun ◽  
...  
Keyword(s):  
Reaction Time ◽  
Styrene Oxide ◽  
Molar Ratio ◽  
Temperature Reaction ◽  
Styrene Epoxidation ◽  
Reaction Conditions ◽  
Reaction Conversion ◽  
Tert Butyl Hydroperoxide ◽  
Optimum Reaction ◽  
Optimized Conditions

Styrene was selectively oxidized to styrene oxide with macrocylic amido Mn (II) complex as catalyst and tert-Butyl hydroperoxide (TBHP) as oxidant. The effects of reaction temperature, reaction time, solvents, amount of catalyst and oxidant on the conversion and selectivity of styrene epoxidation were investigated. The optimized conditions were achieved by molar ratio of n (catalyst) :n (styrene)=1% in acetonitrile solvent at 75 °C in 1.5 h. Under optimum reaction conditions, reaction conversion of 92.6% and selectivity of 86.9 % were obtained.

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