By Georgios M. Kopanos, Pei Liu, Michael C. Georgiadis
This publication offers a systematic framework for built-in ideas to advanced power difficulties. It adopts a holistic, systems-based method of show the possibility of an strength structures engineering method of systematically quantify assorted suggestions at numerous degrees of complexity (technology, plant, strength provide chain, mega-system). using modeling, simulation and optimization-based frameworks, besides a few real-life functions, it makes a speciality of complex power structures together with power provide chains, built-in biorefineries, power making plans and scheduling methods and concrete strength systems.
Featuring contributions from best researchers within the box, this paintings turns out to be useful for lecturers, researchers, practitioners in strength structures engineering, and all people who are interested in model-based strength systems.
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Additional info for Advances in Energy Systems Engineering
Kopanos et al. 1007/978-3-319-42803-1_2 21 22 J. Gao et al. S. 6 % per year from 2012 to 2040. S. total natural gas production from shale gas is expected to increase to 53 % by 2040. The remarkable development of large-scale shale gas production would not be possible without the hydraulic fracturing and horizontal drilling technologies (Gregory et al. 2011; Vengosh et al. 2013). Different from the conventional natural gas, shale gas is embedded in the shale rocks that can be a few thousand feet deep.
Although methane is still the dominant component in wet gas, the amount of NGLs is signiﬁcant enough to require further processing. Depending on the location, both the estimated ultimate recovery (EUR) and shale gas composition of a shale well may have signiﬁcant variance. All of these issues render the optimal design and operation in the shale gas industry a challenging topic. Apart from the shale gas itself, the wide application of hydraulic fracturing has resulted in another serious issue, known as the shale water management problem (Nicot and Scanlon 2012; Mauter et al.
Are successively taken from the dry gas using an NGL cutting unit. The C2 and C3 hydrocarbons in the remaining steam are then sent to an oleﬁn separation unit followed by an oleﬁn production unit. Meanwhile, the H2-rich gas goes through a pressure swing adsorption (PSA) unit for hydrogen recovery. Next, methane from the NGL cutting unit is sent to the methane-to-ethylene area and then partially oxidized via the oxidative coupling of methane (OCM) reaction in an O2-rich environment. The OCM product includes ethylene, ethane, hydrogen, carbon dioxide, carbon monoxide, and unconverted methane.