Abstract
This paper reports on the application of low-grade sensible waste heat (liquid phase) driven multi-effect distillation (MED) technology to exploit waste heat sources that are generally abundant in the petrochemical industries especially, those located close to the Persian Gulf's coastline. For this purpose, a techno-economic feasibility study by considering local capital and operating costs for a selected petrochemical plant has been conducted. In this study, a sensible waste heat stream (practically at 80 °C in the liquid phase), which is actively cooled by the cooling process of the plant, is considered as the heat source for the proposed desalination process. This process can recover around 10% of the boiler-grade water demand (namely 644 m3/day out of 6000 m3/day) of the selected petrochemical plant. A detailed capital and operating costs and cash flow analysis are presented to show the economic viability of this kind of waste heat source for desalination purpose in petrochemical industries in Iran. Our study points to a net present value of 1.46 million USD with about 4.5 year payback period at a discount rate of 15%.
Original language | English |
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Journal | Desalination |
DOIs | |
Publication status | E-pub ahead of print - 8 Jul 2019 |
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An industrial application of low-grade sensible waste heat driven seawater desalination : A case study. / Rahimi, B.; Marvi, Z.; Alamolhoda, Ali Asghar; Tehranifard, Majid Abbaspour; Chua, Hui Tong.
In: Desalination, 08.07.2019.Research output: Contribution to journal › Article
TY - JOUR
T1 - An industrial application of low-grade sensible waste heat driven seawater desalination
T2 - A case study
AU - Rahimi, B.
AU - Marvi, Z.
AU - Alamolhoda, Ali Asghar
AU - Tehranifard, Majid Abbaspour
AU - Chua, Hui Tong
PY - 2019/7/8
Y1 - 2019/7/8
N2 - This paper reports on the application of low-grade sensible waste heat (liquid phase) driven multi-effect distillation (MED) technology to exploit waste heat sources that are generally abundant in the petrochemical industries especially, those located close to the Persian Gulf's coastline. For this purpose, a techno-economic feasibility study by considering local capital and operating costs for a selected petrochemical plant has been conducted. In this study, a sensible waste heat stream (practically at 80 °C in the liquid phase), which is actively cooled by the cooling process of the plant, is considered as the heat source for the proposed desalination process. This process can recover around 10% of the boiler-grade water demand (namely 644 m3/day out of 6000 m3/day) of the selected petrochemical plant. A detailed capital and operating costs and cash flow analysis are presented to show the economic viability of this kind of waste heat source for desalination purpose in petrochemical industries in Iran. Our study points to a net present value of 1.46 million USD with about 4.5 year payback period at a discount rate of 15%.
AB - This paper reports on the application of low-grade sensible waste heat (liquid phase) driven multi-effect distillation (MED) technology to exploit waste heat sources that are generally abundant in the petrochemical industries especially, those located close to the Persian Gulf's coastline. For this purpose, a techno-economic feasibility study by considering local capital and operating costs for a selected petrochemical plant has been conducted. In this study, a sensible waste heat stream (practically at 80 °C in the liquid phase), which is actively cooled by the cooling process of the plant, is considered as the heat source for the proposed desalination process. This process can recover around 10% of the boiler-grade water demand (namely 644 m3/day out of 6000 m3/day) of the selected petrochemical plant. A detailed capital and operating costs and cash flow analysis are presented to show the economic viability of this kind of waste heat source for desalination purpose in petrochemical industries in Iran. Our study points to a net present value of 1.46 million USD with about 4.5 year payback period at a discount rate of 15%.
KW - Desalination
KW - Freshwater
KW - Heat recovery
KW - MED
KW - Persian gulf
KW - Waste heat
UR - http://www.scopus.com/inward/record.url?scp=85068451091&partnerID=8YFLogxK
U2 - 10.1016/j.desal.2019.06.021
DO - 10.1016/j.desal.2019.06.021
M3 - Article
JO - Desalination
JF - Desalination
SN - 0011-9164
ER -