Article Outline
Synonyms
Indices
Sets
Parameters
Variables
Introduction
Definition
Formulation
Material Balance Constraints for Product-Stock Tank j
Capacity Constraints
Allocation Constraints
Demand Constraints
Sequence Constraints
Duration Constraints
Blending Stage Consideration
Material Balance Constraints for the Blender
Material Balance Constraints for Component Tank l
Allocation Constraints for Product-Stock Tank j
Allocation Constraints for Blender
Sequence Constraints
Duration Constraints
Objective Function
Case
Conclusions
References
This is a preview of subscription content, log in via an institution.
Buying options
Tax calculation will be finalised at checkout
Purchases are for personal use only
Learn about institutional subscriptionsReferences
DeWitt CW, Lasdon LS, Waren AD, Brenner DA, Melhem SA (1989) Omega: an improved gasoline blending system for Texaco. Interfaces 19:85
Dujkanovic M, Babic B, Milosevic B, Sobajic DJ, Pao YH (1996) Fuzzy linear programming based optimal fuel scheduling incorporating blending/transloading facilities. IEEE Trans Power Syst 11:1017
Floudas CA, Lin X (2004) Continuous-Time versus Discrete-Time Approaches for Scheduling of Chemical Processes: A Review. Comput Chem Eng 28:2109
Floudas CA, Lin X (2005) Mixed Integer Linear Programming in Process Scheduling: Modeling, Algorithms, and Applications. Ann Oper Res 139:131
Glismann K, Gruhn G (2001) Short-term planning of blending processes: scheduling and nonlinear optimization of recipes. Chem Eng Tech 24:246
Glismann K, Gruhn G (2001) Short-term scheduling and recipe optimization of blending processes. Comput Chem Eng 25:627
Ierapetritou MG, Floudas CA (1998) Effective Continuous-Time Formulation for Short-Term Scheduling. 1. Multipurpose Batch Processes. Ind Eng Chem Res 37:4341
Ierapetritou MG, Floudas CA (1998) Effective Continuous-Time Formulation for Short-Term Scheduling. 2. Continuous and Semicontinuous Processes. Ind Eng Chem Res 37:4360
Ierapetritou MG, Hene TS, Floudas CA (1999) Effective Continuous-Time Formulation for Short Term Scheduling. 3. Multiple Intermediate Due Dates. Ind Eng Chem Res 38:3446
Jia Z, Ierapetritou MG, Kelly JD (2003) Refinery short-term scheduling using continuous time formulation – crude oil operations. Ind Eng Chem Res 42:3085
Kelly JD. Honeywell Hi-Spec Solutions. Personal communication
Quesada I, Grossmann IE (1995) Global optimization of bilinear process network with multicomponent flows. Comput Chem Eng 19:1219
Rigby B, Lasdon LS, Waren AD (1995) The evolution of Texaco blending systems - from omega to starblend. Interfaces 25:64
Singh A, Forbes JF, Vermeer PJ, Woo SS (2000) Model-based real-time optimization of automotive gasoline blending operations. J Process Control 10:43
Author information
Authors and Affiliations
Editor information
Editors and Affiliations
Rights and permissions
Copyright information
© 2008 Springer-Verlag
About this entry
Cite this entry
Jia, Z., Ierapetritou, M. (2008). Gasoline Blending and Distribution Scheduling: An MILP Model . In: Floudas, C., Pardalos, P. (eds) Encyclopedia of Optimization. Springer, Boston, MA. https://doi.org/10.1007/978-0-387-74759-0_195
Download citation
DOI: https://doi.org/10.1007/978-0-387-74759-0_195
Publisher Name: Springer, Boston, MA
Print ISBN: 978-0-387-74758-3
Online ISBN: 978-0-387-74759-0
eBook Packages: Mathematics and StatisticsReference Module Computer Science and Engineering