TY  - JOUR
PB  - Elsevier Ltd
SN  - 03605442
EP  - 195
AV  - none
SP  - 190
TI  - A combined process integration and fuel switching strategy for emissions reduction in chemical process plants
N1  - cited By 33
Y1  - 2009///
VL  - 34
JF  - Energy
A1  - Mahmoud, A.
A1  - Shuhaimi, M.
A1  - Abdel Samed, M.
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-60449100627&doi=10.1016%2fj.energy.2008.11.007&partnerID=40&md5=861897f18a1057480e056bf1b6cd338a
ID  - scholars807
KW  - Acid rain; Air pollution; Carbon dioxide; Chemical engineering; Combustion; Crude petroleum; Distillation; Distillation equipment; Emission control; Flue gases; Fossil fuels; Fuels; Gas emissions; Global warming; Heat exchangers; Investments; Retrofitting; Smoke; Sulfur; Sulfur dioxide; Switching; Thermochemistry
KW  -  Atmospheric pollutions; Capital investments; Chemical process plants; Combined methods; Combined process; Combustion products; Crude oil; Emissions reduction; Flue-gas emissions; Fuel switching; Heat exchanger networks; Oxides of nitrogens; Payback periods; Process heating; Retrofit of HEN
KW  -  Leakage (fluid)
KW  -  acid rain; atmospheric pollution; carbon dioxide; chemical process; emission control; global warming; heating; nitrogen oxides; strategic approach
IS  - 2
N2  - The combustion of fossil fuel to provide process heating is the major source of atmospheric pollution. Combustion products such as carbon dioxide, oxides of sulfur, oxides of nitrogen and particulates are known to be the major causes for global warming, acid rains and smog. This paper presents a combined method of fuel switching and heat exchanger network (HEN) retrofit to reduce flue gas emissions. The method is demonstrated using pre-heat train of a crude oil distillation unit as the case study. Target emissions reduction of 50 is achieved at an approximate payback period of 0.44 year on the capital investment due to the combination of the two methods. © 2009.
ER  -