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Dive into the research topics where S. Chandra Shekar is active.

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Featured researches published by S. Chandra Shekar.


Applied Catalysis A-general | 2003

Selective hydrogenolysis of dichlorodifluoromethane (CCl2F2) over CCA supported palladium bimetallic catalysts

S. Chandra Shekar; J. Krishna Murthy; P. Kanta Rao; K.S. Rama Rao; Erhard Kemnitz

Abstract La, Bi, Sb, Sn, Ba, and Zn are chosen for addition on carbon covered alumina (CCA) supported Pd catalyst. The effect of these second metals on supported Pd catalysts has been studied for the hydrogenolysis activity of CCl 2 F 2 . Bi and Sb promoters have been found to improve not only the thermal stability but also selectivity towards CH 2 F 2 . Sn bimetallic catalyst exhibited high selectivity towards CHClF 2 . This may be explained on the basis of the metal–metal interactions that influence the reducibility of the palladium. These improved properties arise due to inter-metallic compound formation as evidenced from the XRD and TPR data on CCA supported bimetallic palladium catalysts. The effect of addition of second metal on Pd/CCA catalyst is screened in terms of partial dehalogenation ability and thermal stability for hydrodechlorination activity of CCl 2 F 2 to maximize the CH 2 F 2 yield.


Catalysis Communications | 2002

Highly selective zirconium oxychloride modified Pd/C catalyst in the hydrodechlorination of dichlorodifluoromethane to difluoromethane

J. Krishna Murthy; S. Chandra Shekar; V. Siva Kumar; K.S. Rama Rao

Zirconium oxychloride modified active carbon supported palladium catalyst appears to be a promising system in the hydrodechlorination of CCl2F2 to yield CH2F2 in greater yields; showing an altogether different product distribution compared to Pd/C and Pd/ZrO2 catalysts. The catalysts have been characterized by BET-surface area, CO-chemisorption, X-ray diffraction (XRD), temperature programmed reduction (TPR) analysis and fluorine contents in used catalysts. The interaction of Zr species with Pd and the formation of fluorinated zirconium species during the course of reaction led to the higher selectivity towards CH2F2.


Chinese Journal of Catalysis | 2016

13X分子筛负载Fe催化剂上1,4-二氧六环在空气中完全氧化

C. Ramakrishna; R. Krishna; T. Gopi; G. Swetha; Bijendra Saini; S. Chandra Shekar; Anchal Srivastava

Abstract Zeolite-13X-supported Fe (Fe/zeolite-13X) catalysts with various Fe contents were prepared by the wet impregnation method. The catalysts were characterized by N2 adsorption-desorption isotherms to estimate the Brunauer–Emmett–Teller surface areas and Barrett–Joyner–Hanlenda pore size distributions. X-ray diffraction, scanning electron microscopy, temperature-programmed reduction, and temperature-programmed desorption of NH3 were used to investigate the textural properties of the Fe/zeolite-13X catalysts. Their catalytic activities were determined for the complete oxidation of 1,4-dioxane using air as the oxidant in a fixed‐bed flow reactor in the temperature range 100–400 °C. The influences of various process parameters, such as reaction temperature, metal loading, and gas hourly space velocity (GHSV), on the dioxane removal efficiency by catalytic oxidation were investigated. The stability of the catalyst was tested at 400 °C by performing time-on-stream analysis for 50 h. The Fe/zeolite-13X catalyst with 6 wt% Fe exhibited the best catalytic activity among the Fe/zeolite-13X catalysts at 400 °C and a GHSV of 24000 h−1, with 97% dioxane conversion and 95% selectivity for the formation of carbon oxides (CO and CO2). Trace amounts (


Studies in Surface Science and Catalysis | 1998

Hydrodechlorination of 1,1,2-Trichloro-1,2,2 trifluoroethane (CFC-113) over Pd supported on modified AL2O3

S. Chandra Shekar; Akula Venugopal; K.S. Rama Rao; P.S. Sai Prasad; R. Srinivas; P. Kanta Rao

Hydrdechlorination (HDC) is to be not only a process for a safe disposal of chlorofluorocarbons (CFCs) but also effective in preparation of useful chemical intermediates. Palladium based catalysts have been found to be very promising in the HDC reactions. It is observed that the nature of support used for the palladium catalysts has a role to play in modifying the selectivity towards useful products. In the present investigation, the influence of modification of the alumina support on the activity and selectivity of Pd catalysts during the HDC of CFC-113 is reported.


Phosphorus Sulfur and Silicon and The Related Elements | 2016

A simple and controlled oxidative decontamination of sulfur mustard and its simulants using ozone gas

C. Ramakrishna; R. Krishna; Bijendra Saini; T. Gopi; G. Swetha; S. Chandra Shekar

GRAPHICAL ABSTRACT ABSTRACT A simple and efficient oxidative decontamination method was developed for sulfur mustard (HD), a potential chemical warfare agent. The method involves treatment of chemical warfare agent HD and its simulants, i.e., dimethyl sulfide, diethyl sulfide, and 2-chloroethyl ethyl sulfide with ozone gas at ambient conditions in acetonitrile solvent. Ozone gas readily oxidizes sulfur mustard in a controlled manner to give its corresponding nontoxic sulfoxide. This transformation is selective and takes place even at subzero temperatures. The oxidation products of HD and its simulants were monitored and quantified by gas chromatography and gas chromatography–mass spectrometry.


Ozone-science & Engineering | 2016

Vapor Phase Selective Catalytic Oxidation of Cyclohexane over 13X Supported Metal Oxides in the Presence of Ozone

T. Gopi; G. Swetha; S. Chandra Shekar; Keshav Soni; R. Krishna; C. Ramakrishna; Bijendra Saini

ABSTRACT This article reports the application of ozone for the selective oxidation of cyclohexane over 13X molecular sieve supported various metal oxides at ambient temperatures. From the SEM, XRD and HR-TEM results, the impregnated metal oxides are highly dispersed on the support. The activity results reveal that Co/MS, Mo/MS, Cu/MS, and Ag/MS catalysts produce cyclohexanone/cyclohexanol as selective oxidation products, whereas Ce/MS, Mn/MS, and V/MS catalysts yield, predominantly, CO and CO2. Among them, Co/MS catalyst exhibits better conversion of 12.2% with selectively of 58% to cyclohexanone/cyclohexanol, which is attributed to the simultaneous activation of ozone and cyclohexane (-C-H bond) at ambient conditions.


Journal of Molecular Catalysis A-chemical | 2003

Selective hydrogenolysis of dichlorodifluoromethane on carbon covered alumina supported palladium catalyst

S. Chandra Shekar; J. Krishna Murthy; P. Kanta Rao; K.S. Rama Rao


Catalysis Communications | 2009

Ozone assisted partial oxidation of DMS to DMSO on Fe based catalyst

S. Chandra Shekar; Keshav Soni; Rajendra Bunkar; Manoj Sharma; Beer Singh; Anil K. Nigam; T.H. Mahato; R. Vijayaraghavan


Catalysis Communications | 2017

Catalytic decomposition of ozone on nanostructured potassium and proton containing δ-MnO2 catalysts

T. Gopi; G. Swetha; S. Chandra Shekar; C. Ramakrishna; Bijendra Saini; R. Krishna; P.V.L. Rao


Catalysis Communications | 2004

Promotional effect of magnesia addition to active carbon supported Pd catalyst on the characteristics and hydrodechlorination activity of CCl2F2

J. Krishna Murthy; S. Chandra Shekar; A.H. Padmasri; Akula Venugopal; V. Siva Kumar; B.M. Nagaraja; V. Shashikala; B. David Raju; P. Kanta Rao; K.S. Rama Rao

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C. Ramakrishna

Defence Research and Development Establishment

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T. Gopi

Defence Research and Development Establishment

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G. Swetha

Defence Research and Development Establishment

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Bijendra Saini

Defence Research and Development Establishment

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K.S. Rama Rao

Indian Institute of Chemical Technology

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Keshav Soni

Defence Research and Development Establishment

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J. Krishna Murthy

Indian Institute of Chemical Technology

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P. Kanta Rao

Indian Institute of Chemical Technology

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Beer Singh

Defence Research and Development Establishment

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V. Siva Kumar

Indian Institute of Chemical Technology

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