@article { ISI:000276973200011, title = {Continuous flow synthesis of functionalized silver nanoparticles using bifunctional biosurfactants}, journal = {Green Chemistry}, volume = {12}, number = {4}, year = {2010}, month = {APR}, pages = {609-615}, publisher = {ROYAL SOC CHEMISTRY}, address = {THOMAS GRAHAM HOUSE, SCIENCE PARK, MILTON RD, CAMBRIDGE CB4 0WF, CAMBS, ENGLAND}, abstract = {

Silver nanoparticles were synthesized by continuous flow methods using biosurfactants, namely, oleic acid sophorolipid (OASL) and stearic acid sophorolipid (SASL). Both the sophorolipids can act as reducing and capping agents. The effect of temperature on the completion of nanoparticle formation and the particle growth dynamics (size) were studied in batch mode. While the completion of the reaction using oleic acid sophorolipid needed 20 min, only 5 min were required with the stearic acid sophorolipid as capping and reducing agent. Hence all the continuous flow experiments were carried out using the stearic acid sophorolipid. The continuous flow synthesis of silver nanoparticles was carried out in a stainless steel helical coil and also in a spiral polymeric minichannel reactor. The DLS results show that higher flow rate leads to the formation of bigger and polydisperse particles because of incomplete reactions. Higher residence time allowed the completion of reaction leading to spherical, small and monodisperse particles.

}, issn = {1463-9262}, doi = {10.1039/b919550e}, author = {Kumar, D. V. Ravi and Kasture, Manasi and Prabhune, Asmita and Ramana, C. V. and Bhagavatula L. V. Prasad and Kulkarni, A. A.} } @article { ISI:000326121800014, title = {Continuous flow multipoint dosing approach for selectivity engineering in sulfoxidation}, journal = {Organic Process Research \& Development}, volume = {17}, number = {10}, year = {2013}, month = {OCT}, pages = {1293-1299}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

A continuous synthesis approach with multipoint dosing of one of the reagents is demonstrated for the synthesis of sulfoxide compounds such as proton pump inhibitors. Use of multipoint dosing of the oxidizing agent helped to minimize the possibility of over-oxidation leading to sulfone. Different oxidizing agents were used, and the effect of various parameters (viz. mole ratio of sulfide to oxidizing agent, temperature, residence time, concentration of oxidizing agent, etc.) on the yield of the desired sulfoxide compound was studied. Single-point and multipoint dosing approaches of the oxidizing agent were used for the most promising set of parameters. The performance was compared in terms of conversion of sulfide and the selectivity of the desired sulfoxide. Numbering up approach was used to produce the sulfoxide in a relatively large quantity at laboratory scale with complete conversion and over 99\% selectivity for the sulfoxide.

}, issn = {1083-6160}, doi = {10.1021/op400138v}, author = {Kulkarni, A. A. and Nivangune, N. T. and Joshi, Rohini R. and Joshi, Ramesh A.} } @article { ISI:000361866400009, title = {Continuous-flow nitration of o-xylene: effect of nitrating agent and feasibility of tubular reactors for scale-up}, journal = {Organic Process Research \& Development}, volume = {19}, number = {9, SI}, year = {2015}, month = {SEP}, pages = {1138-1147}, publisher = {AMER CHEMICAL SOC}, address = {1155 16TH ST, NW, WASHINGTON, DC 20036 USA}, abstract = {

Continuous-flow nitration of o-xylene has been studied with different nitrating agents over a wide range of conditions for different parameters such as temperature, residence time, and concentrations. A nitrating mixture comprising sulfuric acid and fuming nitric acid was seen to yield higher selectivity for the isomer 1,2-dimethyl-3-nitrobenzene over the isomer 1,2-dimethyl-4-nitrobenzene and also a non-negligible quantity of dinitro derivatives of o-xylene. With only fuming nitric acid as the nitrating agent, the reaction was selective for 1,2-dimethyl-4-nitrobenzene over 1,2-dimethyl-3-nitrobenzene. Impurities mainly come from nitration of mononitro derivatives, and this occurs more from nitration of the 3-nitro isomer because of its higher reactivity with nitric acid. An economic analysis of the continuous-flow reactor for the production of 1,2-dimethyl-4-nitrobenzene at 100 and 500 kg/h in a jacketed tubular reactor showed that numbering-up is a more economical approach for higher production capacity. A combination of large- and small-sized tubes depending upon the relative rates of heat generation during a reaction will achieve more profit and a shorter payback period than having the entire reactor made of a single tube size.

}, issn = {1083-6160}, doi = {10.1021/acs.oprd.5b00064}, author = {Sharma, Y. and Joshi, Ramesh A. and Kulkarni, A. A.} }