Kandukuri S. Gandhi
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Kandukuri S. Gandhi has a total of 75 co-authors. Here are the top co-authors by number of shared publications:
R. Kumar
Department of Chemical Engineering, Indian Institute of Science, Bangalore 560012, India
39 shared publications- Sanjeev Kumar
Indian Institute of Science Bangalore
8 shared publications T.R. Das
4 shared publicationsDebdarsan Niyogi
TATA Consultancy Services Limited, 33 Grosvenor Place, London SW1X 7HY, U.K.
3 shared publicationsDoraiswami Ramkrishna
3 shared publicationsR. Rajan
Department of Chemical Engineering, Indian Institute of Science, Bangalore-560 012, India
3 shared publications
Latest Publications
- Open Access
- 14 April 2017
- Published by The Electrochemical Society in Journal of the Electrochemical Society
- Vol. 164 (11) , E3092-E3101
Modeling of Effect of Double-Layer Capacitance and Failure of Lead-Acid Batteries in HRPSoC Application
Lead-acid batteries fail faster in partial state-of-charge start-stop technology than in SLI application. Accumulation of lead sulfate on negative electrode’s surface has been identified as the cause. It is also known that life can be enhanced by increasing capacitance of negative electrode. A bench-marking test cycle is used to explain these observations through a one-dimensional model. It is shown that, at the large discharge current densities used, faradaic reactions in the electrodes are spatially inhomogeneous, and charging is unable to reverse its effects. Consequently, lead sulfate deposit is larger on electrode’s surface than at its center. Model uses a rate expression for charging modified to include diffusion of Pb2 +, and predicts that sulfate continues to accumulate with cycling. A portion of electrode becomes inactive when volume fraction of sulfate reaches a critical value there. Battery fails when inactive area becomes large. It is shown that double-layer capacitance suppresses the non-uniformity in the faradaic reaction and alters the pattern of accumulation of sulfate. Negative electrode does not benefit from this since its capacitance is low. Sulfate accumulates in positive electrode also, but does not reach critical levels since positive electrode’s capacitance is large. This explains the life enhancing effect of capacitance.
- 14 April 2017
- Published by The Electrochemical Society in Journal of the Electrochemical Society
- Vol. 164 (11) , E3092-E3101
Open AccessModeling of Effect of Double-Layer Capacitance and Failure of Lead-Acid Batteries in HRPSoC Application
Lead-acid batteries fail faster in partial state-of-charge start-stop technology than in SLI application. Accumulation of lead sulfate on negative electrode’s surface has been identified as the cause. It is also known that life can be enhanced by increasing capacitance of negative electrode. A bench-marking test cycle is used to explain these observations through a one-dimensional model. It is shown that, at the large discharge current densities used, faradaic reactions in the electrodes are spatially inhomogeneous, and charging is unable to reverse its effects. Consequently, lead sulfate deposit is larger on electrode’s surface than at its center. Model uses a rate expression for charging modified to include diffusion of Pb2 +, and predicts that sulfate continues to accumulate with cycling. A portion of electrode becomes inactive when volume fraction of sulfate reaches a critical value there. Battery fails when inactive area becomes large. It is shown that double-layer capacitance suppresses the non-uniformity in the faradaic reaction and alters the pattern of accumulation of sulfate. Negative electrode does not benefit from this since its capacitance is low. Sulfate accumulates in positive electrode also, but does not reach critical levels since positive electrode’s capacitance is large. This explains the life enhancing effect of capacitance.
- 1 July 2015
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 54 (42) , 10520-10529
Strategy for Obtaining Bimodal Bubble Size Distribution in Water Blown Polyurethane Foams
- 1 July 2015
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 54 (42) , 10520-10529
Strategy for Obtaining Bimodal Bubble Size Distribution in Water Blown Polyurethane Foams
- 15 May 2015
- Published by The Electrochemical Society in Journal of the Electrochemical Society
- Vol. 162 (8) , A1506-A1515
Modeling of Effect of Nucleation Rate and Electrodes’ Resistance on Discharge Characteristics of Lead-Acid Batteries
Classical models are not successful in describing discharge characteristics of a lead-acid battery when the current density is varied over a wide range. A model is developed in this work to overcome this lacuna by introducing into the standard models two mechanisms that have not been used earlier. Lead sulfate particles nucleate and grow on active materials of electrodes during discharge, resulting in coverage of active area. Increasing rate of discharge builds supersaturation of lead sulfate rapidly, and causes increased extents of nucleation and coverage. Electrodes behave almost like an insulator due to deposition of lead sulfate when active materials are converted to a critical extent, and this can stop discharge process. Influence of this mechanism is also rate dependent. The new model developed is tested against data on polarization behavior, and capacity drawn as a function of current. The model successfully predicts both polarization curves and Peukert behavior. The model is used to predict charge that can be drawn at a current after partial discharge at a different current. Model suggests that altering nucleation behavior can be useful in enhancing capacity available for discharge.
- 15 May 2015
- Published by The Electrochemical Society in Journal of the Electrochemical Society
- Vol. 162 (8) , A1506-A1515
Modeling of Effect of Nucleation Rate and Electrodes’ Resistance on Discharge Characteristics of Lead-Acid Batteries
Classical models are not successful in describing discharge characteristics of a lead-acid battery when the current density is varied over a wide range. A model is developed in this work to overcome this lacuna by introducing into the standard models two mechanisms that have not been used earlier. Lead sulfate particles nucleate and grow on active materials of electrodes during discharge, resulting in coverage of active area. Increasing rate of discharge builds supersaturation of lead sulfate rapidly, and causes increased extents of nucleation and coverage. Electrodes behave almost like an insulator due to deposition of lead sulfate when active materials are converted to a critical extent, and this can stop discharge process. Influence of this mechanism is also rate dependent. The new model developed is tested against data on polarization behavior, and capacity drawn as a function of current. The model successfully predicts both polarization curves and Peukert behavior. The model is used to predict charge that can be drawn at a current after partial discharge at a different current. Model suggests that altering nucleation behavior can be useful in enhancing capacity available for discharge.
- 1 March 2015
- Published by Elsevier in Journal of Power Sources
- Vol. 277, 124-130
Role of electrical resistance of electrodes in modeling of discharging and charging of flooded lead-acid batteries
- 1 March 2015
- Published by Elsevier in Journal of Power Sources
- Vol. 277, 124-130
Role of electrical resistance of electrodes in modeling of discharging and charging of flooded lead-acid batteries
- 14 April 2014
- Published by Wiley in Journal of Applied Polymer Science
- Vol. 131 (18)
Modeling of bubble‐size distribution in water and freon co‐blown free rise polyurethane foams
A model has been developed to simulate the foam characteristics obtained, when chemical (water) and physical (Freon) blowing agents are used together for the formation of polyurethane foams. The model considers the rate of reaction, the consequent rise in temperature of the reaction mixture, nucleation of bubbles, and mass transfer of CO2 and Freon to them till the time of gelation. The model is able to explain the experimental results available in literature. It further predicts that the nucleation period gets reduced with increase in water (at constant Freon content), whereas with increase in Freon (at constant water) concentration nucleation period decreases marginally leading to narrower bubble‐size distribution. By the use of uniform sized nuclei added initially, the model predicts that the bubble‐size distribution can be made independent of the rate of homogeneous nucleation and can, thus, offer an extra parameter for its control. © 2014 Wiley Periodicals, Inc. J. Appl. Polym. Sci. 2014, 131, 40745.
- 14 April 2014
- Published by Wiley in Journal of Applied Polymer Science
- Vol. 131 (18)
Modeling of bubble‐size distribution in water and freon co‐blown free rise polyurethane foams
A model has been developed to simulate the foam characteristics obtained, when chemical (water) and physical (Freon) blowing agents are used together for the formation of polyurethane foams. The model considers the rate of reaction, the consequent rise in temperature of the reaction mixture, nucleation of bubbles, and mass transfer of CO2 and Freon to them till the time of gelation. The model is able to explain the experimental results available in literature. It further predicts that the nucleation period gets reduced with increase in water (at constant Freon content), whereas with increase in Freon (at constant water) concentration nucleation period decreases marginally leading to narrower bubble‐size distribution. By the use of uniform sized nuclei added initially, the model predicts that the bubble‐size distribution can be made independent of the rate of homogeneous nucleation and can, thus, offer an extra parameter for its control. © 2014 Wiley Periodicals, Inc. J. Appl. Polym. Sci. 2014, 131, 40745.
- 20 September 2012
- Published by Wiley in AIChE Journal
- Vol. 58 (11) , 3601-3605
Use of Fick's law and Maxwell–Stefan equations in computation of multicomponent diffusion
- 20 September 2012
- Published by Wiley in AIChE Journal
- Vol. 58 (11) , 3601-3605
Use of Fick's law and Maxwell–Stefan equations in computation of multicomponent diffusion
- 22 July 2009
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 48 (21) , 9755-9762
Modeling of Freezing Phenomena Induced by Chemical Reactions
- 22 July 2009
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 48 (21) , 9755-9762
Modeling of Freezing Phenomena Induced by Chemical Reactions
- 1 January 2009
- Published by The Electrochemical Society in Journal of the Electrochemical Society
- Vol. 156 (3) , A238-A245
Simplified Mathematical Model for Effects of Freezing on the Low-Temperature Performance of the Lead-Acid Battery
Discharge periods of lead-acid batteries are significantly reduced at subzero centigrade temperatures. The reduction is more than what can be expected due to decreased rates of various processes caused by a lowering of temperature and occurs despite the fact that active materials are available for discharge. It is proposed that the major cause for this is the freezing of the electrolyte. The concentration of acid decreases during battery discharge with a consequent increase in the freezing temperature. A battery freezes when the discharge temperature falls below the freezing temperature. A mathematical model is developed for conditions where charge-transfer reaction is the rate-limiting step, and Tafel kinetics are applicable. It is argued that freezing begins from the midplanes of electrodes and proceeds toward the reservoir in-between. Ionic conduction stops when one of the electrodes freezes fully and the time taken to reach that point, namely the discharge period, is calculated. The predictions of the model compare well to observations made at low current density (C/5) and at −20−20 and −40°C−40°C . At higher current densities, however, diffusional resistances become important and a more complicated moving boundary problem needs to be solved to predict the discharge periods.
- 1 January 2009
- Published by The Electrochemical Society in Journal of the Electrochemical Society
- Vol. 156 (3) , A238-A245
Simplified Mathematical Model for Effects of Freezing on the Low-Temperature Performance of the Lead-Acid Battery
Discharge periods of lead-acid batteries are significantly reduced at subzero centigrade temperatures. The reduction is more than what can be expected due to decreased rates of various processes caused by a lowering of temperature and occurs despite the fact that active materials are available for discharge. It is proposed that the major cause for this is the freezing of the electrolyte. The concentration of acid decreases during battery discharge with a consequent increase in the freezing temperature. A battery freezes when the discharge temperature falls below the freezing temperature. A mathematical model is developed for conditions where charge-transfer reaction is the rate-limiting step, and Tafel kinetics are applicable. It is argued that freezing begins from the midplanes of electrodes and proceeds toward the reservoir in-between. Ionic conduction stops when one of the electrodes freezes fully and the time taken to reach that point, namely the discharge period, is calculated. The predictions of the model compare well to observations made at low current density (C/5) and at −20−20 and −40°C−40°C . At higher current densities, however, diffusional resistances become important and a more complicated moving boundary problem needs to be solved to predict the discharge periods.
- 10 November 2007
- Published by American Chemical Society (ACS) in Langmuir
- Vol. 23 (26) , 12795-12798
Enhancing the Hydrophobic Effect in Confined Water Nanodrops
The distribution of hydrophobic solutes, such as methane, enclosed in a nanosized water droplet contained in a reverse micelle of diameter 2.82 nm is investigated using Monte Carlo simulations. The effect of the hydrophobic solute's atomic diameter on the solute-solute potential of mean force is also studied. The study reveals that confinement has a strong influence on the solute's tendency to associate. The potential of mean force exhibits only a single minimum, indicating that the contact pair is the only stable configuration between solutes. The solvent-separated pair that is universally observed for small solutes in bulk water is conspicuously absent. This enhanced hydrophobic effect is attributed to the lack of sufficient water to completely hydrate and stabilize the solvent-separated configurations. The study is expected to be important in understanding the role of hydrophobic forces during protein folding and nucleation under confinement.
- 10 November 2007
- Published by American Chemical Society (ACS) in Langmuir
- Vol. 23 (26) , 12795-12798
Enhancing the Hydrophobic Effect in Confined Water Nanodrops
The distribution of hydrophobic solutes, such as methane, enclosed in a nanosized water droplet contained in a reverse micelle of diameter 2.82 nm is investigated using Monte Carlo simulations. The effect of the hydrophobic solute's atomic diameter on the solute-solute potential of mean force is also studied. The study reveals that confinement has a strong influence on the solute's tendency to associate. The potential of mean force exhibits only a single minimum, indicating that the contact pair is the only stable configuration between solutes. The solvent-separated pair that is universally observed for small solutes in bulk water is conspicuously absent. This enhanced hydrophobic effect is attributed to the lack of sufficient water to completely hydrate and stabilize the solvent-separated configurations. The study is expected to be important in understanding the role of hydrophobic forces during protein folding and nucleation under confinement.
- 7 October 2006
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 46 (10) , 3128-3136
Modeling of Formation of Gold Nanoparticles by Citrate Method
- 7 October 2006
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 46 (10) , 3128-3136
Modeling of Formation of Gold Nanoparticles by Citrate Method