2020
DOI: 10.1016/j.tsep.2019.100381
|View full text |Cite
|
Sign up to set email alerts
|

Thermo-economic optimization of a nanofluid based organic Rankine cycle: A multi-objective study and analysis

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1
1
1
1

Citation Types

0
5
0

Year Published

2021
2021
2023
2023

Publication Types

Select...
6
1

Relationship

1
6

Authors

Journals

citations
Cited by 24 publications
(5 citation statements)
references
References 34 publications
0
5
0
Order By: Relevance
“…An analogy can be made with exceptional heat transfer properties and operational costs; with higher efficiency, the return-on-investment increases. Prajapati and Patel [121] performed the thermoeconomic optimization of the nanofluid-based organic Rankine cycle and observed that the enhancement of the thermal transfer properties due to the introduction of nanofluids shortened the payback period. Some of the widely used heat transfer fluids, such as water, air, hydrocarbon oils, and refrigerants, are abundant and cheap but require processing which is one of the major contributors to the operating costs of the process plant.…”
Section: Comparing Different Commercial Heat Transfer Fluidsmentioning
confidence: 99%
“…An analogy can be made with exceptional heat transfer properties and operational costs; with higher efficiency, the return-on-investment increases. Prajapati and Patel [121] performed the thermoeconomic optimization of the nanofluid-based organic Rankine cycle and observed that the enhancement of the thermal transfer properties due to the introduction of nanofluids shortened the payback period. Some of the widely used heat transfer fluids, such as water, air, hydrocarbon oils, and refrigerants, are abundant and cheap but require processing which is one of the major contributors to the operating costs of the process plant.…”
Section: Comparing Different Commercial Heat Transfer Fluidsmentioning
confidence: 99%
“…Assuming the Hex has negligible heat loss to its surroundings, the fluid's properties are deemed constant, and there is negligible tube wall thermal resistance. Q remains constant throughout the Hex, and it is possible to calculate the overall heat transfer coefficient with Equation (): Ugoodbreak=1hi+1ho1 where h i and h o represent the convection heat transfer coefficient of water and ethylene glycol, respectively, and are calculated using Equations () [ 60 ] : italicRegoodbreak=ρvdμ italicPrgoodbreak=Cpμk italicNugoodbreak=0.023Re0.8Pr0.4,0.25emitalicRe>104,0.25em0.6Pr160 higoodbreak=NukD The pressure drop p generated by the fluid in the pipes can be calculated using Equations () [ 60,74 ] : pgoodbreak=italicfρv2L2D fgoodbreak=0.79lnRe1.642,0.25em3000italicRe5goodbreak×106 vgoodbreak=4trueṁitalicρπD2 The pumping power is calculated with Equation (): …”
Section: Simplified Heat Transfer Modelmentioning
confidence: 99%
“…The pressure drop Δp generated by the fluid in the pipes can be calculated using Equations ( 7)-( 9) [60,74] :…”
Section: Evaluation Of Initial Heat Transfer and Operational Parametersmentioning
confidence: 99%
“…A multiobjective heat transfer search (MOHTS) is a multiobjective variant of the HTS algorithm capable to handle two or more objectives simultaneously. [36][37][38][39][40][41][42][43][44][45] The MOHTS algorithm works on the nondominating principle. The algorithm produces a set of solutions for each objective, from which the dominating solutions are eliminated and nondominating solutions are stored in external archives.…”
Section: E Modeling Of Power Cycle and Objective Function Formulationmentioning
confidence: 99%