ResearchSpace

On energy optimisation in multipurpose batch plants using heat storage

Show simple item record

dc.contributor.author Majozi, T
dc.contributor.author Stamp, J
dc.date.accessioned 2014-08-27T05:54:06Z
dc.date.available 2014-08-27T05:54:06Z
dc.date.issued 2010-10
dc.identifier.citation Majozi, T and Stamp, J. 2010. On energy optimisation in multipurpose batch plants using heat storage. In: 13th Asia Pacific Confederation of Chemical Engineering Congress (APCChE 2010), Taipei, Taiwan, 5-8 October 2010 en_US
dc.identifier.uri http://hdl.handle.net/10204/7637
dc.description 13th Asia Pacific Confederation of Chemical Engineering Congress (APCChE 2010), Taipei, Taiwan, 5-8 October 2010 en_US
dc.description.abstract The use of heat integration in multipurpose batch plants to minimise energy usage has been in the literature for more than two decades. Direct heat integration may be exploited when the heat source and heat sink processes are active over a common time interval. Indirect heat integration makes use of a heat transfer fluid for storing energy and allows heat integration of processes regardless of the time interval. This is possible as long as the source process takes place before the sink process thus allowing heat to be stored for later use. In both cases, heat transfer may only take place if the thermal driving forces allow. The use of heat storage instead of only direct heat integration leads to increased flexibility in the process and therefore improved energy usage. For present methods, the schedule tends to be fixed and as such, time is also fixed a priori, leading to sub-optimal results. The method presented in this paper treats time as a variable and consequently leads to improved results. Both direct and indirect heat integration are considered as well as the optimisation of the heat storage size and the initial temperature of the heat storage fluid. The mathematical formulation is based on an uneven discretization of the time horizon and the state sequence network (SSN) recipe representation. The resulting model exhibits the mixed integer nonlinear programming (MINLP) structure, which implies that global optimality cannot generally be guaranteed. However, a procedure is presented that seeks to find a globally optimal solution, even for nonlinear problems. en_US
dc.language.iso en en_US
dc.relation.ispartofseries Workflow;5075
dc.subject Heat integration en_US
dc.subject Heat storage en_US
dc.subject Multipurpose en_US
dc.subject Multiproduct en_US
dc.subject Energy optimisation en_US
dc.title On energy optimisation in multipurpose batch plants using heat storage en_US
dc.type Conference Presentation en_US
dc.identifier.apacitation Majozi, T., & Stamp, J. (2010). On energy optimisation in multipurpose batch plants using heat storage. http://hdl.handle.net/10204/7637 en_ZA
dc.identifier.chicagocitation Majozi, T, and J Stamp. "On energy optimisation in multipurpose batch plants using heat storage." (2010): http://hdl.handle.net/10204/7637 en_ZA
dc.identifier.vancouvercitation Majozi T, Stamp J, On energy optimisation in multipurpose batch plants using heat storage; 2010. http://hdl.handle.net/10204/7637 . en_ZA
dc.identifier.ris TY - Conference Presentation AU - Majozi, T AU - Stamp, J AB - The use of heat integration in multipurpose batch plants to minimise energy usage has been in the literature for more than two decades. Direct heat integration may be exploited when the heat source and heat sink processes are active over a common time interval. Indirect heat integration makes use of a heat transfer fluid for storing energy and allows heat integration of processes regardless of the time interval. This is possible as long as the source process takes place before the sink process thus allowing heat to be stored for later use. In both cases, heat transfer may only take place if the thermal driving forces allow. The use of heat storage instead of only direct heat integration leads to increased flexibility in the process and therefore improved energy usage. For present methods, the schedule tends to be fixed and as such, time is also fixed a priori, leading to sub-optimal results. The method presented in this paper treats time as a variable and consequently leads to improved results. Both direct and indirect heat integration are considered as well as the optimisation of the heat storage size and the initial temperature of the heat storage fluid. The mathematical formulation is based on an uneven discretization of the time horizon and the state sequence network (SSN) recipe representation. The resulting model exhibits the mixed integer nonlinear programming (MINLP) structure, which implies that global optimality cannot generally be guaranteed. However, a procedure is presented that seeks to find a globally optimal solution, even for nonlinear problems. DA - 2010-10 DB - ResearchSpace DP - CSIR KW - Heat integration KW - Heat storage KW - Multipurpose KW - Multiproduct KW - Energy optimisation LK - https://researchspace.csir.co.za PY - 2010 T1 - On energy optimisation in multipurpose batch plants using heat storage TI - On energy optimisation in multipurpose batch plants using heat storage UR - http://hdl.handle.net/10204/7637 ER - en_ZA


Files in this item

This item appears in the following Collection(s)

Show simple item record