Techno-economic analysis of combined concentrating solar power and desalination plant configurations in Israel and Jordan

被引：50

作者：

Olwig, Ralf ^{[2
,3
]}

Hirsch, Tobias ^{[2
,3
]}

Sattler, Christian ^{[2
,3
]}

Glade, Heike ^{[1
]}

Schmeken, Louisa ^{[1
]}

Will, Stefan ^{[1
]}

Ghermandi, Andrea ^{[4
]}

Messalem, Rami ^{[4
]}

机构：

[1] Univ Bremen, D-28359 Bremen, Germany

[2] German Aerosp Ctr, Inst Tech Thermodynam, D-51147 Cologne, Germany

[3] German Aerosp Ctr, Inst Tech Thermodynam, D-70569 Stuttgart, Germany

[4] Ben Gurion Univ Negev, Zuckerberg Inst Water Res, IL-84105 Beer Sheva, Israel

来源：

DESALINATION AND WATER TREATMENT | 2012年 / 41卷 / 1-3期

关键词：

Desalination; Solar energy; Reverse osmosis; Multi-effect distillation; Concentrating solar power; Costs of water; REVERSE-OSMOSIS;

D O I：

10.1080/19443994.2012.664674

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Combined concentrating solar power (CSP) and desalination plants represent a realistic future option for the production of electricity and fresh water for countries of the world's sunbelt. In this paper, parabolic trough power plants for electricity production have been analysed in combination with multi-effect distillation (MED) and ultrafiltration/reverse osmosis (RO) desalination plants for two sites in Israel (Ashdod) and Jordan (Aqaba). Both RO and MED desalination plants were designed for a fresh water production capacity of 24,000 m(3)/d. The power block of the CSP plant was selected to meet the steam consumption of the MED plant at the design point, which led to a gross electrical power generation capacity of the power block of 42 MWel,gross. Due to the low availability and generally high cost of coastal land, the CSP + RO plant consists of two separate units. It was assumed that the CSP plant is located at an inland location where there is land available. The RO plant is located at the sea, while the MED plant is located at the CSP site. The pumping of the seawater and the water transmission system add about 0.2 $/m(3) to the levelized water costs of the CSP + MED plant compared with a plant located at the sea. Three different sizes of high temperature heat storages (0h, 6h and 12h of additional full load operation of the steam turbine) were applied to find the most economic setup. At current prices for heat storage units, systems with huge heat storage capacities become economic only at high feed-in tariffs for electricity and thus high revenues. The price of the electricity generated by the CSP plant was varied to show the influence of the feed-in tariff on the water generating costs. The levelized costs of water (LCOW) strongly depend on the electricity price. Water costs in Ashdod are higher than those in Aqaba due to the lower solar irradiance. For Aqaba, LCOW of about 1 $/m(3) can be realized if a feed-in tariff of about 0.24 $/kWh for electricity from renewable energy sources is established.

引用

页码：9 / 25

页数：17

共 18 条

[1]

Adas H., 2008, P EUROMED C DES COOP

[2]

Cable R. G., 1998, Proceedings of the International Solar Energy Conference. Solar Engineering 1998, P445

[3]

DOW Water Solutions, 2008, FILMTEC REV OSM MEMB

[4] State-of-the-art of reverse osmosis desalination [J].

Fritzmann, C. ;

Loewenberg, J. ;

Wintgens, T. ;

Melin, T. .

DESALINATION, 2007, 216 (1-3) :1-76

[5]

Geyer M, 2006, P 13 SOLARPACES S SE

[6]

Glueckstern P., 2008, 2 CAN ISR IND RES DE

[7]

Kuckelkorn T., 2009, P SOLARPACES C BERL

[8] Ultrafiltration membrane pre-treatment benefits for reverse osmosis process in seawater desalting. Quantification in terms of capital investment cost and operating cost reduction [J].

Lorain, Olivier ;

Hersant, Berengere ;

Persin, Francoise ;

Grasmick, Alain ;

Brunard, Nathalie ;

Espenan, Jean Michel .

DESALINATION, 2007, 203 (1-3) :277-285

[9]

LUPFERT E, 2001, P ASME INT SOL EN C, P389

[10]

Middle East Desalination Research Center (MEDRC), 2006, REV OSM WAT TREATM S

← 1 2 →