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Dive into the research topics where Karan H. Mistry is active.

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Featured researches published by Karan H. Mistry.


Entropy | 2011

Entropy Generation Analysis of Desalination Technologies

Karan H. Mistry; Ronan K. McGovern; Gregory P. Thiel; Edward K. Summers; Syed M. Zubair; John H. Lienhard

Increasing global demand for fresh water is driving the development and implementation of a wide variety of seawater desalination technologies. Entropy generation analysis, and specifically, Second Law efficiency, is an important tool for illustrating the influence of irreversibilities within a system on the required energy input. When defining Second Law efficiency, the useful exergy output of the system must be properly defined. For desalination systems, this is the minimum least work of separation required to extract a unit of water from a feed stream of a given salinity. In order to evaluate the Second Law efficiency, entropy generation mechanisms present in a wide range of desalination processes are analyzed. In particular, entropy generated in the run down to equilibrium of discharge streams must be considered. Physical models are applied to estimate the magnitude of entropy generation by component and individual processes. These formulations are applied to calculate the total entropy generation in several desalination systems including multiple effect distillation, multistage flash, membrane distillation, mechanical vapor compression, reverse osmosis, and humidification-dehumidification. Within each technology, the relative importance of each source of entropy generation is discussed in order to determine which should be the target of entropy generation minimization. As given here, the correct application of Second Law efficiency shows which systems operate closest to the reversible limit and helps to indicate which systems have the greatest potential for improvement.


Entropy | 2013

Generalized Least Energy of Separation for Desalination and Other Chemical Separation Processes

Karan H. Mistry; John H. Lienhard

Increasing global demand for fresh water is driving the development and implementation of a wide variety of seawater desalination technologies driven by different combinations of heat, work, and chemical energy. This paper develops a consistent basis for comparing the energy consumption of such technologies using Second Law efficiency. The Second Law efficiency for a chemical separation process is defined in terms of the useful exergy output, which is the minimum least work of separation required to extract a unit of product from a feed stream of a given composition. For a desalination process, this is the minimum least work of separation for producing one kilogram of product water from feed of a given salinity. While definitions in terms of work and heat input have been proposed before, this work generalizes the Second Law efficiency to allow for systems that operate on a combination of energy inputs, including fuel. The generalized equation is then evaluated through a parametric study considering work input, heat inputs at various temperatures, and various chemical fuel inputs. Further, since most modern, large-scale desalination plants operate in cogeneration schemes, a methodology for correctly evaluating Second Law efficiency for the desalination plant based on primary energy inputs is demonstrated. It is shown that, from a strictly energetic point of view and based on currently available technology, cogeneration using electricity to power a reverse osmosis system is energetically superior to thermal systems such as multiple effect distillation and multistage flash distillation, despite the very low grade heat input normally applied in those systems.


Desalination and Water Treatment | 2013

An improved model for multiple effect distillation

Karan H. Mistry; Mohamed A. Antar; John H. Lienhard

Abstract Increasing global demand for fresh water is driving research and development of advanced desalination technologies. As a result, a detailed model of multiple effect distillation (MED) is developed that is flexible, simple to implement, and suitable for use in optimization of water and power cogeneration systems. The MED system is modeled in a modular method in which each of the subcomponents is modeled individually and then instantiated as necessary in order to piece together the complete plant model. Modular development allows for studying various MED configurations (such as forward feed, parallel feed, etc.) with minimal code duplication. Use of equation-oriented solvers, such as Engineering Equation Solver and JACOBIAN, rather than sequential solvers, simplifies the coding complexity dramatically and also reduces the number of required approximations and assumptions. The developed model is compared with four prominent forward feed MED models from literature. Through parametric analysis, it is ...


Entropy | 2013

An Economics-Based Second Law Efficiency

Karan H. Mistry; John H. Lienhard

Second Law efficiency is a useful parameter for characterizing the energy requirements of a system in relation to the limits of performance prescribed by the Laws of Thermodynamics. However, since energy costs typically represent less than 50% of the overall cost of product for many large-scale plants (and, in particular, for desalination plants), it is useful to have a parameter that can characterize both energetic and economic effects. In this paper, an economics-based Second Law efficiency is defined by analogy to the exergetic Second Law efficiency and is applied to several desalination systems. It is defined as the ratio of the minimum cost of producing a product divided by the actual cost of production. The minimum cost of producing the product is equal to the cost of the primary source of energy times the minimum amount of energy required, as governed by the Second Law. The analogy is used to show that thermodynamic irreversibilities can be assigned costs and compared directly to non-energetic costs, such as capital expenses, labor and other operating costs. The economics-based Second Law efficiency identifies costly sources of irreversibility and places these irreversibilities in context with the overall system costs. These principles are illustrated through three case studies. First, a simple analysis of multistage flash and multiple effect distillation systems is performed using available data. Second, a complete energetic and economic model of a reverse osmosis plant is developed to show how economic costs are influenced by energetics. Third, a complete energetic and economic model of a solar powered direct contact membrane distillation system is developed to illustrate the true costs associated with so-called free energy sources.


Desalination Sustainability#R##N#A Technical, Socioeconomic, and Environmental Approach | 2017

Thermodynamics, Exergy, and Energy Efficiency in Desalination Systems

John H. Lienhard; Karan H. Mistry; Mostafa H. Sharqawy; Gregory P. Thiel

Desalination is the thermodynamic process of separating fresh water from water that contains dissolved salts. This chapter introduces the concepts and methods required for thermodynamic analysis of desalination systems. Thermodynamic laws are summarized along with the chemical thermodynamics of electrolytes. Exergy analysis is introduced. The work and heat of separation are defined, and the roles of entropy generation and exergy destruction are identified. Important sources of entropy generation are discussed. Examples are given for the application of these methods to several representative desalination systems.


Volume 3: Advanced Composite Materials and Processing; Robotics; Information Management and PLM; Design Engineering | 2012

Prognosis of Component Degradation Under Uncertainty: A Method for Early Stage Design of a Complex Engineering System

Bo Yang Yu; Tomonori Honda; Gina M. Zak; Alexander Mitsos; Karan H. Mistry; Syed M. Zubair; Mostafa H. Sharqawy; Mohamed Abdelkerim Antar; John H. Lienhard; Maria C. Yang

This paper proposes a method that dynamically improves a statistical model of system degradation by incorporating uncertainty. The method is illustrated by a case example of fouling, or degradation, in a heat exchanger in a cogeneration desalination plant. The goal of the proposed method is to select the best model from several representative condenser fouling models including linear, falling rate, and asymptotic fouling, and to validate and improve model parameters over the duration of operation. Maximum likelihood estimation (MLE) was applied to obtain a stochastic distribution of condenser fouling. Akaike’s Information Criterion (AIC) and the Bayesian Information Criterion (BIC) were then computed at time intervals to assess the accuracy of the MLE results. The degradation model was further evaluated by estimating future prognoses and then cross-validating with real world fouling data. The results show the accuracy of a prognosis can be improved substantially by continuously updating fouling model parameters. The proposed method is a step toward facilitating prognosis of engineering systems in the early design stages by improving the prediction of future component degradation.Copyright


International Journal of Thermal Sciences | 2010

Effect of entropy generation on the performance of humidification-dehumidification desalination cycles

Karan H. Mistry; John H. Lienhard; Syed M. Zubair


Frontiers in Heat and Mass Transfer | 2010

ENERGY EFFECTIVENESS OF SIMULTANEOUS HEAT AND MASS EXCHANGE DEVICES

G. Prakash Narayan; Karan H. Mistry; Mostafa H. Sharqawy; Syed M. Zubair; John H. Lienhard


International Journal of Thermal Sciences | 2011

Optimal operating conditions and configurations for humidification–dehumidification desalination cycles

Karan H. Mistry; Alexander Mitsos; John H. Lienhard


Desalination | 2013

Effect of composition and nonideal solution behavior on desalination calculations for mixed electrolyte solutions with comparison to seawater

Karan H. Mistry; Harrison A. Hunter; John H. Lienhard

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John H. Lienhard

Massachusetts Institute of Technology

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Syed M. Zubair

King Fahd University of Petroleum and Minerals

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Mostafa H. Sharqawy

King Fahd University of Petroleum and Minerals

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Gregory P. Thiel

Massachusetts Institute of Technology

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Prakash Narayan Govindan

King Fahd University of Petroleum and Minerals

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Bo Yang Yu

Massachusetts Institute of Technology

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David Elan Martin Warsinger

Massachusetts Institute of Technology

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Edward K. Summers

Massachusetts Institute of Technology

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G. Prakash Narayan

Massachusetts Institute of Technology

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