Optimization of Organic Rankine Cycle Waste Heat Recovery for Power Generation in a Cement Plant via Response Surface Methodology

2015 ◽  
Vol 6 (6) ◽  
pp. 938 ◽  
Author(s):  
Hendi Riyanto ◽  
Sigit Yoewono Martowibowo
Energy ◽  
2014 ◽  
Vol 64 ◽  
pp. 462-472 ◽  
Author(s):  
Mohammed A. Khatita ◽  
Tamer S. Ahmed ◽  
Fatma. H. Ashour ◽  
Ibrahim M. Ismail

2019 ◽  
Vol 142 (2) ◽  
Author(s):  
Zineb Fergani ◽  
Tatiana Morosuk ◽  
Djamel Touil

Abstract In this paper, the potential application of an organic Rankine cycle (ORC) for cogeneration in a cement plant is presented. Two ORC system configurations are considered. The first configuration is based on the waste heat recovery from the exit gases of clinker burning system. An additional heat source which is the solar energy was used for the second configuration. Parametric studies are performed for the systems with three different working fluids. Both systems are optimized from the viewpoints of thermodynamic, exergoeconomic, and exergoenvironmental analyses.


2021 ◽  
Author(s):  
Shantanu Thada ◽  
Yash T. Rajan ◽  
A. M. Pradeep ◽  
Arunkumar Sridharan

Abstract The accelerating growth of electricity demand necessitates looking for potential waste heat recovery solutions in production industries. Significant potential for efficient waste heat recovery is observed in the cement manufacturing industry. Based on the waste heat source temperatures in a cement plant, two potential candidates, the supercritical CO2 Brayton (S-CO2) cycle or the Organic Rankine cycle (ORC), promises low capital cost and enhanced thermodynamic performance. The current study focuses on modelling and optimization of the S-CO2 and ORC cycles for a 1 MTPA cement plant, with the raw-clinker preheater as the waste-heat source. The primary objective is to maximize the net-power output using genetic algorithms. A comparative performance analysis of the two ORCs with working fluids: R134a and Propane, the simply recuperated S-CO2 cycle (RC) and recompressed-recuperated S-CO2 cycle (RRC) configurations is presented with varying number of preheaters. For all cases, ORC-R134a yields more power than the ORC-Propane, RC, and RRC configurations. In terms of the waste heat recovered, ORC-Propane marginally outperforms ORC-R134a. The ORC configurations recover 32%–38% of the available heat, while the S-CO2 configurations recover, at maximum, 25%–30% of the available heat.


Author(s):  
Frederick J. Cogswell ◽  
David W. Gerlach ◽  
Timothy C. Wagner ◽  
Jarso Mulugeta

A 5-kW Organic Rankine Cycle (ORC) was designed for mobile 60-kW diesel engine waste heat recovery applications to provide additional electricity for powering air conditioners. The ORC uses a non-flammable, near-zero-global-warming-potential fluid (Novec649) in a supercritical cycle. The system conceptual design and some observations on the component specification are described. The system will utilize an advanced oil-free high speed direct drive turbine. The proposed power generation module has a volume of ∼3 ft3 and contains the turbine, generator, pump, recuperator, and electrical components. The heat rejection heat exchanger is located on the power generation module in a configuration similar to mini-split air conditioners. The heat recovery heat exchanger (supercritical heater) is attached to the diesel generator and placed in series before the OEM muffler. The supercritical heater must be carefully designed to prevent the refrigerant from overheating, while still maintaining a high effectiveness.


2021 ◽  
Vol 11 (5) ◽  
pp. 1984
Author(s):  
Ramin Moradi ◽  
Emanuele Habib ◽  
Enrico Bocci ◽  
Luca Cioccolanti

Organic Rankine cycle (ORC) systems are some of the most suitable technologies to produce electricity from low-temperature waste heat. In this study, a non-regenerative, micro-scale ORC system was tested in off-design conditions using R134a as the working fluid. The experimental data were then used to tune the semi-empirical models of the main components of the system. Eventually, the models were used in a component-oriented system solver to map the system electric performance at varying operating conditions. The analysis highlighted the non-negligible impact of the plunger pump on the system performance Indeed, the experimental results showed that the low pump efficiency in the investigated operating range can lead to negative net electric power in some working conditions. For most data points, the expander and the pump isentropic efficiencies are found in the approximate ranges of 35% to 55% and 17% to 34%, respectively. Furthermore, the maximum net electric power was about 200 W with a net electric efficiency of about 1.2%, thus also stressing the importance of a proper selection of the pump for waste heat recovery applications.


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