2007
DOI: 10.1016/j.jclepro.2005.08.004
|View full text |Cite
|
Sign up to set email alerts
|

Effective MILP model for oil refinery-wide production planning and better energy utilization

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
39
0

Year Published

2008
2008
2016
2016

Publication Types

Select...
6
2

Relationship

1
7

Authors

Journals

citations
Cited by 59 publications
(39 citation statements)
references
References 11 publications
0
39
0
Order By: Relevance
“…Fixed thermal efficiency of process heaters is widely used to calculate the fuel requirements of process units [41]. To obtain more accurate thermal efficiency, Eq.…”
Section: Fuel Requirements Based On Pinch Analysismentioning
confidence: 99%
See 1 more Smart Citation
“…Fixed thermal efficiency of process heaters is widely used to calculate the fuel requirements of process units [41]. To obtain more accurate thermal efficiency, Eq.…”
Section: Fuel Requirements Based On Pinch Analysismentioning
confidence: 99%
“…The structure of utility systems was then formulated and integrated into a total site model [39,40]. The energy requirements of process units were further correlated with operating conditions and seasonal changes in Zhang and Hua [41]. Driven by rising energy prices, more accurate models of turbines and heaters were integrated into site models to optimize materials and energy simultaneously [42].…”
Section: Introductionmentioning
confidence: 99%
“…The rectifying FI (FIr) is used if the temperature is greater than the component boiling temperature; otherwise, the stripping FI (FIs) is used. The following disjunction represents the FI choice, (10) where Yi,j,cr,t is the Boolean (binary) decision variable, γi,j,cr,t is a placeholder for the FI value, Tb,i is the component boiling point and Tj,cr,t is the cut point temperature.…”
Section: Fi Modelmentioning
confidence: 99%
“…The need for more accurate nonlinear representations of the process units as well as integrated planning and scheduling refinery operation models are recognized as key future challenges in the field 5,7,8,9 . Multiperiod refinery planning models tend to utilize linear equations for the process units 10,11,12 . The nonlinear implementation for the process unit in multiperiod planning models rely mainly on empirical relations 13 .…”
Section: Introductionmentioning
confidence: 99%
“…Davis (2004) and White (2005) proposed the concept of the fuel gas balance and recommended to model the planning model of the site-wide energy system integrating fuel gas, steam and electricity. Zhang and Hua (2007) embedded the MILP (mixed integer linear programming) model of utility system which included the fuel gas system into the plant-wide planning model for c h e m i c a l e n g i n e e r i n g r e s e a r c h a n d d e s i g n 8 6 ( 2 0 0 8 ) 1 4 1 -1 5 1…”
Section: Introductionmentioning
confidence: 99%