2017
DOI: 10.1016/j.energy.2016.11.089
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Pumped thermal energy storage and bottoming system part A: Concept and model

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Cited by 39 publications
(11 citation statements)
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“…During the charging process of the energy storage, heat is pumped from cold reservoirs (CRs) to hot reservoirs (HRs) via a heat pump circle and then stored; during the discharging process electricity is generated by the stored thermal energy through the heat-work conversion circle. Owning to the advantages of its high energy density and high efficiency, PHES has captured the attention of researchers as a promising technology for large-scale energy storage in recent years [14][15][16][17][18][19][20][21][22][23][24][25][26][27][28][29][30][31]. The categories of the PHES systems is mainly based on two types of reversible heat-work conversion circles thus far: The Joule-Brayton cycles [25][26][27][28][29][30][31] and the Rankine cycles [14][15][16][17][18][19][20][21][22][23][24].…”
Section: Introductionmentioning
confidence: 99%
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“…During the charging process of the energy storage, heat is pumped from cold reservoirs (CRs) to hot reservoirs (HRs) via a heat pump circle and then stored; during the discharging process electricity is generated by the stored thermal energy through the heat-work conversion circle. Owning to the advantages of its high energy density and high efficiency, PHES has captured the attention of researchers as a promising technology for large-scale energy storage in recent years [14][15][16][17][18][19][20][21][22][23][24][25][26][27][28][29][30][31]. The categories of the PHES systems is mainly based on two types of reversible heat-work conversion circles thus far: The Joule-Brayton cycles [25][26][27][28][29][30][31] and the Rankine cycles [14][15][16][17][18][19][20][21][22][23][24].…”
Section: Introductionmentioning
confidence: 99%
“…Under the situations in this study, the maximum absolute value of angular acceleration of the expander rotor and the compressor rotor is 0.0063 rad/s2 and 0.0026 rad/s2 respectively, and the corresponding Pe(t) and Pc(t) is -3.47 kW and 0.36 kW, which are less than ±0.04% of the transient shaft power and can be neglected. By bringing equation (3), (4) into equation (15), (16), and neglecting the unsteady variation of the turbine machines, the transient specific energy can be calculated using equation (19) for the charging process and equation (20)for the discharging process. Where echr and edis are specific energy (J/kg) of shaft work during charging and discharging, Tc,in and Te,in are the inflow temperatures (K) of the compressor and the expander during charging, and the superscript are many, could be arranged.…”
mentioning
confidence: 99%
“…For systems operating at high pressures, however, the packed-bed containment vessel becomes very expensive. Alternatives include the use a heat exchanger embedded within a solid block [28] or a packed bed with indirect heat transfer, employing a secondary heat exchange fluid [29]. For the first of these, the heat exchanger size is linked to the energy (rather than power) capacity, such that it is likely to be prohibitively expensive for systems with long discharge duration.…”
Section: Storage Mediamentioning
confidence: 99%
“…The vast majority of proposed transcritical cycles run on carbon dioxide [2]- [7]. The reasons usually cited are that carbon dioxide is low cost, widely available, safe to handle and has low impact on the environment, with high density which allows for a more compact and hence cheaper system.…”
Section: Introductionmentioning
confidence: 99%