Influences of additives on the gas hydrate cool storage process in a new gas hydrate cool storage system

2006 ◽  
Vol 47 (18-19) ◽  
pp. 2974-2982 ◽  
Author(s):  
Yuehong Bi ◽  
Tingwei Guo ◽  
Tingying Zhu ◽  
Liang Zhang ◽  
Lingen Chen
Keyword(s):  
Gas Hydrate ◽  
Storage System ◽  
Storage Process ◽  
Cool Storage

Influence of volumetric-flow rate in the crystallizer on the gas-hydrate cool-storage process in a new gas-hydrate cool-storage system

2004 ◽  
Vol 78 (1) ◽  
pp. 111-121 ◽  
Author(s):  
Yuehong Bi ◽  
Tingwei Guo ◽  
Tingying Zhu ◽  
Shuanshi Fan ◽  
Deqing Liang ◽  
...  
Keyword(s):  
Flow Rate ◽  
Gas Hydrate ◽  
Storage System ◽  
Volumetric Flow Rate ◽  
Storage Process ◽  
Cool Storage

Exergy analysis of a gas-hydrate cool storage system

Energy ◽  
2014 ◽  
Vol 73 ◽  
pp. 908-915 ◽  
Author(s):  
Yuehong Bi ◽  
Xiao Liu ◽  
Minghe Jiang
Keyword(s):  
Gas Hydrate ◽  
Exergy Analysis ◽  
Storage System ◽  
Cool Storage

scholarly journals Study on Enhanced Heat Transfer of the Gas Hydrate Storage Tank in the Cool Storage Process

2015 ◽  
Vol 121 ◽  
pp. 1076-1082 ◽  
Author(s):  
Zibiao Wang ◽  
Tingting Fan ◽  
Wei Xiong ◽  
Fengxue Li ◽  
Bo Yang
Keyword(s):  
Heat Transfer ◽  
Gas Hydrate ◽  
Storage Tank ◽  
Storage Process ◽  
Enhanced Heat Transfer ◽  
Cool Storage

Entropy generation minimization for charging and discharging processes in a gas-hydrate cool storage system

2010 ◽  
Vol 87 (4) ◽  
pp. 1149-1157 ◽  
Author(s):  
Yuehong Bi ◽  
Tingwei Guo ◽  
Liang Zhang ◽  
Lingen Chen ◽  
Fengrui Sun
Keyword(s):  
Entropy Generation ◽  
Gas Hydrate ◽  
Storage System ◽  
Entropy Generation Minimization ◽  
Cool Storage ◽  
Charging And Discharging Processes

Using the fuzzy multi-criteria model to select the optimal cool storage system for air conditioning

2008 ◽  
Vol 40 (11) ◽  
pp. 2059-2066 ◽  
Author(s):  
Jiang-Jiang Wang ◽  
Chun-Fa Zhang ◽  
You-Yin Jing ◽  
Guo-Zhong Zheng
Keyword(s):  
Air Conditioning ◽  
Storage System ◽  
Cool Storage ◽  
Optimal Cool

The MSU Micellar-Solution Gas Hydrate Storage Process for Natural Gas

2006 ◽  
pp. 185-198 ◽  
Author(s):  
Rudy E. Rogers ◽  
Yu Zhong ◽  
John A. Etheridge ◽  
Larry E. Pearson
Keyword(s):  
Natural Gas ◽  
Gas Hydrate ◽  
Micellar Solution ◽  
Storage Process ◽  
Solution Gas

scholarly journals Exergy Analysis for Utilizing Latent Energy of Thermal Energy Storage System in District Heating

Energies ◽  
2019 ◽  
Vol 12 (7) ◽  
pp. 1391 ◽  
Author(s):  
Joong Yong Yi ◽  
Kyung Min Kim ◽  
Jongjun Lee ◽  
Mun Sei Oh
Keyword(s):  
Power Generation ◽  
Energy Storage ◽  
Thermal Energy ◽  
Exergy Analysis ◽  
Heat Storage ◽  
Storage System ◽  
District Heating ◽  
Hydraulic Turbine ◽  
Storage Process ◽  
Exergy Losses

The thermal energy storage (TES) system stores the district heating (DH) water when the heating load is low. Since a TES system stores heat at atmospheric pressure, the DH water temperature of 115 °C has to be lowered to less than 100 °C. Therefore, the temperature drop of the DH water results in thermal loss during storage. In addition, the DH water must have high pressure to supply heat to DH users a long distance from the CHP plant. If heat is to be stored in the TES system, a pressure drop in the throttling valve occurs. These exergy losses, which occur in the thermal storage process of the general TES system, can be analyzed by exergy analysis to identify the location, cause and the amount of loss. This study evaluated the efficiency improvement of a TES system through exergy calculation in the heat storage process. The method involves power generation technology using the organic Rankine cycle (ORC) and a hydraulic turbine. As a result, the 930 kW capacity ORC and the 270 kW capacity hydraulic turbine were considered suitable for a heat storage system that stores 3000 m3/h. In this case, each power generation facility was 50% of the thermal storage capacity, which was attributed to the variation of actual heat storage from the annual operating pattern analysis. Therefore, it was possible to produce 1200 kW of power by recovering the exergy losses. The payback period of the ORC and the hydraulic turbine will be 3.5 and 7.13 years, respectively.

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