Heat integration analysis for an industrial ethylbenzene plant using pinch analysis

2007 ◽  
Vol 27 (5-6) ◽  
pp. 886-893 ◽  
Author(s):  
Sung-Geun Yoon ◽  
Jeongseok Lee ◽  
Sunwon Park
Keyword(s):  
Heat Integration ◽  
Pinch Analysis ◽  
Integration Analysis

Heat Integration Analysis and Optimization for a Post Combustion Co2 Capture Retrofit Study of Saskpower's Shand Power Station

2019 ◽  
Author(s):  
Stavroula Giannaris ◽  
Brent Jacobs ◽  
Wayuta Srisang ◽  
Corwyn Bruce ◽  
Dominika Janowczyk
Keyword(s):  
Co2 Capture ◽  
Heat Integration ◽  
Power Station ◽  
Integration Analysis

Thermal integration analysis and improved configuration for multiple effect evaporator system based on pinch analysis

REAKTOR ◽  
2021 ◽  
Vol 21 (2) ◽  
pp. 74-93
Author(s):  
Indra Riadi ◽  
Zulfan Adi Putra ◽  
Heri Cahyono
Keyword(s):  
Production Capacity ◽  
Energy Utilization ◽  
Wash Water ◽  
Plant Production ◽  
Pinch Analysis ◽  
Multiple Effect ◽  
Pressure Steam ◽  
Sugar Plant ◽  
Energy Consumptions ◽  
Integration Analysis

Pinch analysis for a sugar plant production capacity 4000 TCD has been carried out to reduce its energy consumptions. The plant has ten evaporators that can be configured to several multiple effect evaporators. It has been running with five-effect evaporator (quintuple) scheme. To maximize energy utilization within the plant, three multiple effect evaporator schemes were evaluated. They are triple effect evaporator, quadruple effect evaporator, and quintuple effect evaporator as the benchmark. The result shows that the quintuple effect evaporator yields the highest energy efficiency by about 10%. Options to achieve such target is to use low pressure steam only for the first effect and to use steam bleeding from the first effect to heat a tertiary juice heater. With this proposed scenario, sugar dryer, wash water RVF unit and wash water HGF unit no longer need external steam for its operation.

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