TY - JOUR
T1 - Hybrid gas turbine-organic Rankine cycle for seawater desalination by reverse osmosis in a hydrocarbon production facility
AU - Eveloy, Valérie
AU - Rodgers, Peter
AU - Qiu, Linyue
N1 - Funding Information:
The financial support of The Petroleum Institute’s research initiation Grant No. RFIP 14324 is gratefully acknowledged.
Publisher Copyright:
© 2015 Elsevier Ltd.
PY - 2015/12
Y1 - 2015/12
N2 - Despite water scarcity, the use of industrial waste heat for seawater desalination has been limited in the Middle East to date. This study evaluates the technical and economic feasibility of integrating on-site gas turbine power generation and reverse osmosis equipment for the production of both electricity and fresh water in a coastal hydrocarbon production facility. Gas turbine exhaust gas waste heat is recovered using an intermediate heat transfer fluid and fed to an organic Rankine cycle evaporator, to generate mechanical power to drive the reverse osmosis high pressure pump. Six candidate organic working fluids are evaluated, namely toluene, benzene, cyclohexane, cyclopentane, n-pentane and R245fa. Thermodynamic and desalination performance are assessed in the harsh climatic and salinity conditions of the Arabian Gulf. The performance metrics considered incorporate electric power and permeate production, thermal and exergy efficiency, specific energy consumption, system size, and permeate quality. Using toluene in the bottoming power cycle, a gain in power generation efficiency of approximately 12% is achieved relative to the existing gas turbine cycle, with an annual average of 2260 m3/h of fresh water produced. Depending upon the projected evolution of local water prices, the investment becomes profitable after two to four years, with an end-of-life net present value of 220-380 million USD, and internal rate of return of 26-48%.
AB - Despite water scarcity, the use of industrial waste heat for seawater desalination has been limited in the Middle East to date. This study evaluates the technical and economic feasibility of integrating on-site gas turbine power generation and reverse osmosis equipment for the production of both electricity and fresh water in a coastal hydrocarbon production facility. Gas turbine exhaust gas waste heat is recovered using an intermediate heat transfer fluid and fed to an organic Rankine cycle evaporator, to generate mechanical power to drive the reverse osmosis high pressure pump. Six candidate organic working fluids are evaluated, namely toluene, benzene, cyclohexane, cyclopentane, n-pentane and R245fa. Thermodynamic and desalination performance are assessed in the harsh climatic and salinity conditions of the Arabian Gulf. The performance metrics considered incorporate electric power and permeate production, thermal and exergy efficiency, specific energy consumption, system size, and permeate quality. Using toluene in the bottoming power cycle, a gain in power generation efficiency of approximately 12% is achieved relative to the existing gas turbine cycle, with an annual average of 2260 m3/h of fresh water produced. Depending upon the projected evolution of local water prices, the investment becomes profitable after two to four years, with an end-of-life net present value of 220-380 million USD, and internal rate of return of 26-48%.
KW - Brayton
KW - Desalination
KW - Economic
KW - Efficiency
KW - Exergy
KW - Gas turbine
KW - ORC
KW - Organic Rankine cycle
UR - http://www.scopus.com/inward/record.url?scp=84946429923&partnerID=8YFLogxK
U2 - 10.1016/j.enconman.2015.10.019
DO - 10.1016/j.enconman.2015.10.019
M3 - Article
AN - SCOPUS:84946429923
SN - 0196-8904
VL - 106
SP - 1134
EP - 1148
JO - Energy Conversion and Management
JF - Energy Conversion and Management
ER -