Assessment of a molten salt heat transfer fluid in a parabolic trough solar field

被引:381
作者
Kearney, D
Herrmann, U
Nava, P
Kelly, P
Mahoney, R
Pacheco, J
Cable, R
Potrovitza, N
Blake, D
Price, H
机构
[1] Kearney & Associates, Vashon, WA 98070 USA
[2] Flabeg Solar Int, D-58070 Cologne, Germany
[3] Nexant Inc, San Francisco, CA 94105 USA
[4] Sandia Natl Labs, Albuquerque, NM 87185 USA
[5] KJC Operating Co, Boron, CA 95316 USA
[6] Natl Renewable Energy Lab, Golden, CO 80401 USA
来源
JOURNAL OF SOLAR ENERGY ENGINEERING-TRANSACTIONS OF THE ASME | 2003年 / 125卷 / 02期
关键词
D O I
10.1115/1.1565087
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 [动力工程及工程热物理]; 0820 [石油与天然气工程];
摘要
An evaluation was carried out to investigate the feasibility of utilizing a molten salt as the heat transfer fluid (HTF) and for thermal storage in a parabolic trough solar field to improve system performance and to reduce the levelized electricity cost. The operating SEGS (Solar Electric Generating Systems located in Mojave Desert, California) plants currently use a high temperature synthetic oil consisting of a eutectic mixture of biphenyl/ diphenyl oxide. The scope of this investigation included examination of known critical issues, postulating solutions or possible approaches where potential problems exist, and the quantification of performance and electricity cost using preliminary cost inputs. The two leading candidates were the so-called solar salt (a binary salt consisting of 60% NaNO3 and 40% KNO3) and a salt sold commercially as HitecXL (a ternary salt consisting of 48% Ca(NO3)(2), 7% NaNO3, and 45% KNO3). Assuming a two-tank storage system and a maximum operation temperature of 450degreesC, the evaluation showed that the levelized electricity cost can be reduced by 14.2% compared to a state-of-the-art parabolic trough plant such as the SEGS plants. If higher temperatures are possible, the improvement may be as high as 17.6%. Thermocline salt storage systems offer even greater benefits.
引用
收藏
页码:170 / 176
页数:7
相关论文
共 8 条
[1]
KEARNEY D, 2002, P SOL 2002 REN NE
[2]
KEARNEY D, 2002, P 11 SOL INT S CONC
[3]
*NEXT INC, 2001, USA IN NITR SALT HTF
[4]
PACHECO JE, 1997, P ASME INT SOL EN C
[5]
Pacheco JE, 2001, SOLAR FORUM 2001
[6]
*PILK SOL INT, 1999, SOL STEAM SYST INV C
[7]
PRICE H, 1995, P ASME JSME JSES INT
[8]
Reilly H.E., 2001, SAND20013674