scholarly journals Recent advances in the methanol carbonylation reaction into acetic acid

2020 ◽  
Vol 402 ◽  
pp. 213078 ◽  
Author(s):  
Philippe Kalck ◽  
Carole Le Berre ◽  
Philippe Serp
2018 ◽  
Vol 14 (2) ◽  
Author(s):  
Nasrin Nemati ◽  
Reza Eslamlueyan

Abstract In recently developed CativaTM process, acetic acid is produced by methanol carbonylation reaction in which a complex interaction among all the major reaction species including iridium, ruthenium, methyl acetate, methyl iodide and water are observed. In this study, a statistical technique of response surface method (RSM) (which is called historical data design algorithm) is applied to investigate the concentration effects of these species on the carbonylation reaction rate. A quartic equation is fitted to the experimental data, and its suitability is examined by several statistical tests. Lack of fit, model F-value, coefficient of determination (R2), adjusted R-squared (Adj.R2) and predicted R-squared (Pre. R2) are respectively equal to 1.65, 182.73, 0.9822, 0.9768 and 0.9263. The validation of the proposed model is investigated by numerical optimization of the design-expert software. The desirability value of the model prediction is 0.94 that indicates the high agreement between the model prediction and the experimental results. The individual and binary effects of the considered parameters on the carbonylation rate are also investigated through the developed model. The steep slope/ curvature of Ir, Ru and water concentrations in perturbation plot indicates the high sensitivity of carbonylation rate to these species. The interaction effects of Ru and water on carbonylation rate show that at water concentration of 7 w/w %, a steep increase occurs in the reaction rate by increasing Ru promoter. Investigating the simultaneous effects of Ru and Ir concentrations on the carbonylation rate indicates that the increase of Ru to Ir molar ratio promotes the reaction rate by enhancing the lability of [Ir(CO)2I3Me]- complex and preventing the production of inactive species of [Ir(CO)2I4]- in the catalytic cycle.


2017 ◽  
Vol 7 (20) ◽  
pp. 4818-4822 ◽  
Author(s):  
Youming Ni ◽  
Lei Shi ◽  
Hongchao Liu ◽  
Wenna Zhang ◽  
Yong Liu ◽  
...  

Halide-free and noble metal-free pyridine-modified H-mordenites exhibit high stability and selectivity in methanol carbonylation to acetic acid.


2018 ◽  
Vol 35 (4) ◽  
pp. 165 ◽  
Author(s):  
Ígor Augusto Negri Donini ◽  
Denise Toledo Bonemer De Salvi ◽  
Fabiana Keiko Fukumoto ◽  
Wilton Rogério Lustri ◽  
Hernane Da Silva Barud ◽  
...  

The present paper discusses the recent advances about the biosynthesis and production of bacterial cellulose (BC), from gram-negative, aerobic and acetic acid Gluconcetobacter xylinus (Gx). The BC differs from his vegetal pair, mainly due his feature of nanometric fibers, as opposed to micrometric feature of vegetal cellulose, are extruded through the cellular wall of Gx, thereby the macroscopic structure of BC is mechanically and physically more resistant, open big opportunities of biological and technological applications, apart from that obtained by vegetal cellulose. The actual challenge is in the grown of production of BC, which deals a superior understanding of his biosynthesis, to makes possible a later genetic-biochemical manipulation derived from recent advances in molecular biology. Are related works using the BC for production of composites and also what is being done of more actual with this biological material.


Author(s):  
Ali Asghar Jafari ◽  
Somayeh Tourani ◽  
Farhad Khorasheh

Abstract This paper deals with mathematical modeling and simulation of methanol carbonylation reactor in acetic acid production plant that consisted of a continuous stirred tank reactor (CSTR), a flash drum, a Joule-Thomson valve, and a condenser. The model was based on material and energy balances that considered liquid-gas mass transfer, thermodynamics, and reactor hydrodynamics. The most important aspect of the model was the selection of an appropriate correlation for prediction of mass transfer coefficient. Several correlations were examined and comparison of the model results with plant data indicated that the correlation reported by Lemoine was most appropriate. The simulation results were found to be in good agreement with plant data and the effects of various operating parameters on the performance of the model such as temperature of reactor from 186 °C to 183.6 °C, CH3I concentration from 3.11 mol% to 2.21 mol% and agitator rotation speed from 62 rpm to 112 rpm were investigated.


2012 ◽  
Vol 554-556 ◽  
pp. 760-763 ◽  
Author(s):  
Bin Ru ◽  
Xin Bao Li ◽  
Ling Jun Zhu ◽  
Guo Hui Xu ◽  
Yue Ling Gu

Gas-phase methanol carbonylation over HMOR catalyst was investigated for the synthesis of dimethyl ether (DME) and acetic acid (HOAc). The results revealed that the selectivity of DME reached 98% and the methanol conversion was 45% under the reaction temperature of 493K. While, the selectivity of HOAc was 30% and the methanol conversion reached 80% when reaction temperature was increased to 573K. TEM, SEM, XRD, N2 physisorbtion, XPS and TG-DTG measurements were performed to characterize the texture and structure of the catalyst. Serious coking on the catalyst surface significantly limited the utilization of unmodified HMOR catalyst in the reaction.


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