Flash recovery system analysis and flashing tank optimization in desalination plants
Flash recovery system analysis and flashing tank optimization in desalination plants
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69
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48
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98
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334
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27
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- Desalination
- Research Article
14
- 10.1002/aesr.202000108
- Mar 8, 2021
- Advanced Energy and Sustainability Research
Steam generation process is closely related to energy conversion and cleaner energy utilization, and the industrial steam is even regarded as the currency of heat with significant social and economic value. Herein, the possible industrial steam generation paths are analyzed based upon thermodynamics analysis, in which fossil fuel, electric, and heat‐pump heating are considered. The large‐temperature‐lift heat‐pump heating for steam generation is proved to be a most reasonable way with high‐efficiency and wide adaptability. Furthermore, a possible system sketch is proposed, in which the heat pump is used for preheating for low‐temperature evaporation and the generated steam can be thus compressed with a steam compressor to the expected high‐temperature (pressure) steam. The key parameters of the heat pump for steam generation are ascertained and the subsequent optimization space is discussed. The results show that the proposed steam‐generation path has clear performance advantages and potential for industrial steam generation, which could be a sustainable heating system for industry.
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21
- 10.1016/j.applthermaleng.2019.113874
- May 28, 2019
- Applied Thermal Engineering
Experimental study on a flash tank integrated with low concentrating PV/T (FT-LCPVT) hybrid system for desalination
- Research Article
12
- 10.1080/01430750.2020.1712242
- Jan 15, 2020
- International Journal of Ambient Energy
ABSTRACT The present research paper shows the use of a flash evaporator coupled with the solar desalination system to improve the distillate output. Here solar desalination system consists of a solar water heater coupled with evacuated tubes, a flash evaporator and a condenser. Also, two sets of experiments have been utilised for the use of a flash chamber with a solar desalination system and a solar still with a solar desalination system. Experimental set-up has been fabricated at Government Polytechnic Ahmedabad, Gujarat and tested for seven days 1st May to 7th May 2019. From the experimental days, it has been found that the distillate output of the solar desalination system with a flash evaporator obtained an average of 13.95 kg as compared with the solar still of 4.29 kg. From the experiments, it has been concluded that the flash evaporator is a possible solution to improve the distillate output of the solar desalination system.
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Gor Optimization for Hybrid System of Distillation Desalination and Hot-Water Flashingcorresponding Author:Xin-Rong Zhangdepartment of Energy and Resources Engineering, College of Engineering, Peking University, Beijing100871, Chinatel:+86-010-62751812e-Mail: Xrzhang@Pku.Edu.Cn
- Book Chapter
- 10.1007/978-3-319-20535-9_5
- Jan 1, 2015
This chapter addresses the description and thermodynamic analysis for the integration of desalination plants into the power cycle described in Chap. 4. The systems chosen for this study combine a Concentrating Solar Power plant using parabolic-trough collector technology for electricity generation with various desalination plants, giving rise to what is known as a parabolic-trough concentrating solar power and desalination (PT-CSP + D) plant. The description of the PT-CSP plant, based on the Andasol-1 (Blanco-Marigorta et al., 2011) commercial plant, is detailed in Chap. 4, showing all the model equations. The desalination technologies selected to combine with the PT-CSP plant were multi-effect distillation (MED) and reverse osmosis (RO), as discussed in Chap. 1. On one hand, the simultaneous production of water and electricity using an RO plant connected to a CSP plant seems the simpler option. On the other hand, the integration of a low-temperature MED (LT-MED) plant is an interesting alternative because it allows replacement of the conventional power-cycle condenser by using exhaust steam as the thermal energy source for the desalination plant. However, to satisfy demand, while providing a certain performance, the LT-MED plant inlet temperature should be around 70 °C (corresponding to 0.031 bar absolute), meaning that the steam does not completely expand through the turbine and therefore the power-cycle efficiency is low compared with a stand-alone electricity-generating plant. This is the reason why another alternative to the MED plant, MED with thermal vapour compression (TVC), is considered. In this case, the steam expands completely in the turbine until it reaches the permitted value for the condenser conditions. However, part of the steam circulating through the turbine is extracted and used as high-pressure steam; this, together with the low-pressure steam coming from one of the MED effects, generates the inlet steam required in the first stage of the desalination plant. Moreover, in this study, a new concept of CSP + MED plants is evaluated (which, until now, has not been studied in published works), a thermally fed LT-MED plant with steam coming from a thermocompressor (LT-MED + TVC). In this case, the low-pressure steam (the entrained vapour) used by the thermocompressor comes from the exhaust steam of a PT-CSP plant instead of one of the MED effects. In each of the systems studied, desalinated water production is evaluated as well as the power and efficiency of the dual thermal solar power and desalinated water cycle.
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