2016
DOI: 10.1002/cjce.22544
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Integrated short‐term scheduling and production planning in an ethylene plant based on Lagrangian decomposition

Abstract: A cracking furnace, which is the major unit involved in ethylene production, produces various petrochemical products ranging from ethylene to pitch and determines the production yield of an ethylene plant. It is essential to consider the operational performances of the cracking furnaces and to incorporate them into the whole plant's planning problem. Facing this challenge, this paper developed an optimization model, which integrates the scheduling problem of upstream cracking furnaces and the operational plann… Show more

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Cited by 17 publications
(10 citation statements)
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“…Other methodologies for facilitating solutions in MINLP formulations of planning and scheduling problems include Lagrangian decomposition techniques (e.g. Mouret et al (2011), Wang et al (2016)), bi-level decomposition methods (e.g. Li and Ierapetritou (2009), Shi et al (2015), Lin and Du (2018)) and rolling horizon methods (e.g.…”
mentioning
confidence: 99%
“…Other methodologies for facilitating solutions in MINLP formulations of planning and scheduling problems include Lagrangian decomposition techniques (e.g. Mouret et al (2011), Wang et al (2016)), bi-level decomposition methods (e.g. Li and Ierapetritou (2009), Shi et al (2015), Lin and Du (2018)) and rolling horizon methods (e.g.…”
mentioning
confidence: 99%
“…The furnace is the key in the ethylene production industry [14] where its performance will determine the yield and quality of ethylene [15] produced. Coke will be formed over time in the furnace coil resulted from the rapid cracking of naphtha feed in the furnace coil.…”
Section: Introductionmentioning
confidence: 99%
“…Olefin plant producing ethylene and propylene utilizing thermal cracking is often defined as the core of petrochemical manufacturing [7,8] due to its significant impact on the industry. The furnace is the primary equipment in the olefin production industry [9] where its safe and stable operation is essential [10,11] to determine the yield and quality of olefin [12] produced Fig. 1 shows the configuration of the steam cracker furnace in the studied plant while Table 1 shows the naphtha feed specification utilized in the steam cracker furnace during the study.…”
Section: Introductionmentioning
confidence: 99%