scholarly journals Energy Conservation in The Petroleum Industry: Process Heat Integration for a Vapour Recovery Unit Using The Pinch Technology.(Dept.P)

2021 ◽  
Vol 13 (1) ◽  
pp. 12-22
Author(s):  
Seham El-Temtamy ◽  
Salah Khalil
Energies ◽  
2020 ◽  
Vol 13 (4) ◽  
pp. 958 ◽  
Author(s):  
Elin Svensson ◽  
Matteo Morandin ◽  
Simon Harvey ◽  
Stavros Papadokonstantakis

The definition of appropriate energy targets for large industrial processes is a difficult task since operability, safety and plant layout aspects represent important limitations to direct process integration. The role of heat exchange limitations in the definition of appropriate energy targets for large process sites was studied in this work. A computational framework was used which allows to estimate the optimal distribution of process stream heat loads in different subsystems and to select and size a site wide utility system. A complex Swedish refinery site is used as a case study. Various system aggregations, representing different patterns of heat exchange limitations between process units and utility configurations were explored to identify trade-offs and bottlenecks for energy saving opportunities. The results show that in spite of the aforementioned limitations direct heat integration still plays a significant role for the refinery energy efficiency. For example, the targeted hot utility demand is reduced by 50–65% by allowing process-to-process heat exchange within process units even when a steam utility system is available for indirect heat recovery. Furthermore, it was found that direct process heat integration is motivated primarily at process unit level, since the heat savings that can be achieved by allowing direct heat recovery between adjacent process units (25–42%) are in the same range as those that can be obtained by combining unit process-to-process integration with site-wide indirect heat recovery via the steam system (27–42%).


2014 ◽  
Vol 57 ◽  
pp. 2743-2751 ◽  
Author(s):  
Elimar Frank ◽  
Heinz Marty ◽  
Lucien Hangartner ◽  
Stefan Minder

2021 ◽  
Vol 118 (2) ◽  
pp. 211-224
Author(s):  
Fenwicks Shombe Musonye ◽  
Hiram Ndiritu ◽  
Robert Kinyua

1988 ◽  
Vol 12 (2-3) ◽  
pp. 189-194 ◽  
Author(s):  
P. Glavič ◽  
Z. Kravanja ◽  
M. Homšak

Energies ◽  
2021 ◽  
Vol 14 (23) ◽  
pp. 8123
Author(s):  
Luca Riboldi ◽  
Marcin Pilarczyk ◽  
Lars O. Nord

An opportunity to decarbonise the offshore oil and gas sector lies in the integration of renewable energy sources with energy storage in a hybrid energy system (HES). Such concept enables maximising the exploitation of carbon-free renewable power, while minimising the emissions associated with conventional power generation systems such as gas turbines. Offshore plants, in addition to electrical and mechanical power, also require process heat for their operation. Solutions that provide low-emission heat in parallel to power are necessary to reach a very high degree of decarbonisation. This paper investigates different options to supply process heat in offshore HES, while the electric power is mostly covered by a wind turbine. All HES configurations include energy storage in the form of hydrogen tied to proton exchange membrane (PEM) electrolysers and fuel cells stacks. As a basis for comparison, a standard configuration relying solely on a gas turbine and a waste heat recovery unit is considered. A HES combined with a waste heat recovery unit to supply heat proved efficient when low renewable power capacity is integrated but unable to deliver a total CO2 emission reduction higher than around 40%. Alternative configurations, such as the utilization of gas-fired or electric heaters, become more competitive at large installed renewable capacity, approaching CO2 emission reductions of up to 80%.


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