@article { ISI:000230713100019, title = {Alkylation of benzene with alpha-olefins over zirconia supported 12-silicotungstic acid}, journal = {Journal of Molecular Catalysis A - Chemical}, volume = {237}, number = {1-2}, year = {2005}, month = {AUG}, pages = {137-145}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

Liquid phase alkylation of benzene to linear alkyl benzene (LAB) with alpha-olefins has been investigated with 12-silicotungstic acid supported on zirconia (STA/ZrO2) as the catalyst. Among the catalysts, 15 wt.\% STA/ZrO2 calcined at 750 degrees C was found to be most active than others in the alkylation reaction. The total amount of acid sites of different STA loaded catalysts were estimated by TPD of NH3 and 15 wt.\% STA/ZrO2 calcined at 750 degrees C was found to have the highest acidity and more active in the reaction. The optimization of reaction conditions of alkylation of benzene with 1-dodecene was performed with 15 wt.\% STA/ZrO2 calcined at 750 degrees C by varying catalyst concentration (1-5 wt.\% of reaction mixture); temperature, 373-423 K and benzene: 1-dodecene (1-dd) molar ratio, 5-15 in a Parr autoclave under N-2 pressure. Under the optimized reaction conditions, conversion of 1-dodecene (50.8\%) gave high selectivity to 2-phenyl dodecane (47.1\%) and the remaining 3-, 4-, 5- and 6-phenyldodecanes in 4 h. The reaction was found to be heterogeneously catalyzed and no contribution from homogeneous (leached) STA into the reaction medium. (c) 2005 Elsevier B.V. All rights reserved.

}, keywords = {1-dodecene, 12-silicotungstic acid, Alkylation, Benzene, LAB, Zirconia}, issn = {1381-1169}, doi = {10.1016/j.molcata.2005.04.042}, author = {Sawant, D. P. and Halligudi, Shivappa B.} } @article { ISI:000238502400034, title = {Shape selective synthesis of long-chain linear alkyl benzene (LAB) with AIMCM-41/beta zeolite composite catalyst}, journal = {Journal of Molecular Catalysis A-Chemical}, volume = {253}, number = {1-2}, year = {2006}, month = {JUL}, pages = {239-244}, publisher = {ELSEVIER SCIENCE BV}, type = {Article}, address = {PO BOX 211, 1000 AE AMSTERDAM, NETHERLANDS}, abstract = {

The liquid-phase alkylation of benzene with long-chain olefins such as 1-decene, 1-octene and 1-dodecene was carried out over AIMCM-41/Beta zeolite composite material as catalyst. The catalyst was prepared by seeding method and characterized by XRD, N-2 sorption, FTIR pyridine adsorption, NH3-TPD and SEM. Powder XRD of AlMCM-41/Beta zeolite composite material showed the co-existence of well-structured microporous and mesophase of AlMCM-41. The typical textural characteristics of micro- and meso-structured phases were observed in the composite material. The effect of temperature, reactant molar ratios and catalyst weight on 1-dodecene conversion and products selectivity was studied. The composite catalyst was found to be the highly selective towards the formation 2-dodecylbenzene. Under the reaction conditions of 120 degrees C, benzene/1-dodecene molar ratio 10 and time 2h, the catalyst gave 48\% dodecene conversion with 76\%, 2-dodecylbenzene selectivity. Significant improvement in catalytic activity has been achieved by composite material as compared to Al-MCM-41. Although zeolite beta and composite material gave similar conversion of dodecene, the composite material showed higher selectivity towards 2-dodecylbenzene, which could be due to higher diffusibility of 2-dodecylbenzene isomer in the composite material. (c) 2006 Elsevier B.V. All rights reserved.

}, keywords = {AIMCM-41/beta zeolite composite, Alkylation, Benzene, long-chain olefins}, issn = {1381-1169}, doi = {10.1016/j.molcata.2006.03.045}, author = {Bordoloi, Ankur and Devassy, Biju M. and Niphadkar, P. S. and Joshi, P. N. and Halligudi, Shivaraj B.} } @article { ISI:000270790500006, title = {Entrainer for batch distillation of acetic acid -water system}, journal = {Journal of Scientific \& Industrial Research}, volume = {68}, number = {10}, year = {2009}, month = {OCT}, pages = {871-875}, publisher = {NATL INST SCIENCE COMMUNICATION}, address = {DR K S KRISHNAN MARG, NEW DELHI 110 012, INDIA}, abstract = {

Acetic acid-water system (AW) poses a challenge in reactive distillation, acetic acid purity and loss of acetic acid in aqueous solutions. Feasible separation of AW has been studied using entrainers but acetic acid loss in lean phase cannot be avoided. This study presents feasible region to operate column with toluene and benzene as entrainer for AW. Liquid-liquid equilibrium data and nature of tie line for ethyl acetate are given priority.

}, keywords = {Acetic acid, Batch distillation, Benzene, Entrainer, Toluene}, issn = {0022-4456}, author = {Gadekar, S. V. and Naik, R. V. and Kaul, S. N.} } @article { ISI:000264521700002, title = {Selective synthesis of cumene by isopropylation of benzene using catalytic membrane reactor}, journal = {Chemical Engineering Journal}, volume = {147}, number = {2-3}, year = {2009}, month = {APR}, pages = {97-101}, publisher = {ELSEVIER SCIENCE SA}, address = {PO BOX 564, 1001 LAUSANNE, SWITZERLAND}, abstract = {

Selective isopropylation of benzene to cumene is demonstrated using catalytic membrane reactor (CMR), to our knowledge for the first time and the performance was evaluated against conventional plug flow reactor (PFR). Almost complete elimination of byproducts like polyalkylated benzene and higher aromatics could be made possible by using CMR. These are present in significant amount when reaction is carried out with PFR. The cumene selectivity increased up to a maximum of 97.25\% by CMR as against 90.05\% with conventional PFR. The effect of reaction parameters that can greatly influence the process economics, such as liquid hourly space velocity (LHSV), reactant mole ratio and catalyst/reactor volume ratio were investigated. Changes in these parameters made for CMR are industrially advantageous. The process by CMR is more economical and ecofriendly than PFR as far as milder process parameters (higher LHSV, lower reactant feed mole ratio, less catalyst require, etc.) and process intensification (reaction and separation in single reactor) are concerned. The study provides new insights for benzene isopropylation reaction. (C) 2008 Elsevier B.V. All rights reserved.

}, keywords = {Benzene, Catalytic membrane reactor, cumene, Diisopropyl benzene, Friedel-Craft alkylation}, issn = {1385-8947}, doi = {10.1016/j.cej.2008.06.035}, author = {Bokade, Vijay V. and Kharul, Ulhas K.} }