One-stage approach for the integrated design of ORC processes and working fluid using PC-SAFT

被引:4
作者
Schilling, Johannes [1 ]
Lampe, Matthias [1 ]
Gross, Joachim [2 ]
Bardow, Andre [1 ]
机构
[1] Rhein Westfal TH Aachen, Chair Tech Thermodynam, D-52056 Aachen, Germany
[2] Stuttgart Univ, Inst Thermodynam & Thermal Proc Engn, Pfaffen Waldring 9, D-70569 Stuttgart, Germany
来源
26TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING (ESCAPE), PT B | 2016年 / 38B卷
关键词
integrated process optimization; fluid selection; CAMD; PC-SAFT; ORC; ORGANIC RANKINE-CYCLE; MOLECULAR DESIGN; SELECTION; SOLVENT; SYSTEMS; OPTIMIZATION; STATE; HEAT; SEPARATION; EQUATION;
D O I
10.1016/B978-0-444-63428-3.50227-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Organic Rankine Cycles (ORC) can transform low-temperature heat into electrical power. To ensure optimal use of a heat source, process and working fluid need to be tailored to the specific application. We present a one-stage approach for the integrated design of ORC process and working fluid, which identifies the optimal working fluid and the corresponding optimal process in a single optimization problem. For this purpose, a process model is combined with a modern thermodynamic model of the working fluid. The process model is based on equilibrium thermodynamics. The perturbed-chain statistical associating fluid theory (PC-SAFT) is used as physically-based thermodynamic model of the working fluid. The fluid model is extended by a group-contribution method based on PC-SAFT to enable Computer-aided molecular design (CAMD) of novel working fluids within the optimization. The full model enables the integrated design of process and working fluid. The optimization is an MINLP problem depending on two kinds of design variables: continuous process variables and integer variables representing the molecular structure of the working fluid. The one-stage approach is exemplified in a case study for a subcritical ORC process. The approach is shown to efficiently identify the optimal working fluid and the corresponding optimal process parameters. Integer cuts are employed to generate a ranked list of candidates.
引用
收藏
页码:1335 / 1340
页数:6
相关论文
共 28 条
[1]  
Adjiman CS, 2014, COMPUT-AIDED CHEM EN, V34, P55
[2]   A review of working fluid and expander selections for organic Rankine cycle [J].
Bao, Junjiang ;
Zhao, Li .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2013, 24 :325-342
[3]   Continuous-Molecular Targeting for Integrated Solvent and Process Design [J].
Bardow, Andre ;
Steur, Klaas ;
Gross, Joachim .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (06) :2834-2840
[4]   A hierarchical method to integrated solvent and process design of physical CO2 absorption using the SAFT- Mie approach [J].
Burger, Jakob ;
Papaioannou, Vasileios ;
Gopinath, Smitha ;
Jackson, George ;
Galindo, Amparo ;
Adjiman, Claire S. .
AICHE JOURNAL, 2015, 61 (10) :3249-3269
[5]   Fluid selection for the Organic Rankine Cycle (ORC) in biomass power and heat plants [J].
Drescher, Ulli ;
Brueggemann, Dieter .
APPLIED THERMAL ENGINEERING, 2007, 27 (01) :223-228
[6]   Methods for multi-objective investment and operating optimization of complex energy systems [J].
Fazlollahi, Samira ;
Mandel, Pierre ;
Becker, Gwenaelle ;
Marechal, Francois .
ENERGY, 2012, 45 (01) :12-22
[7]   Chemical product design: challenges and opportunities [J].
Gani, R .
COMPUTERS & CHEMICAL ENGINEERING, 2004, 28 (12) :2441-2457
[8]   Perturbed-chain SAFT: An equation of state based on a perturbation theory for chain molecules [J].
Gross, J ;
Sadowski, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (04) :1244-1260
[9]   Exergy based fluid selection for a geothermal Organic Rankine Cycle for combined heat and power generation [J].
Heberle, Florian ;
Brueggemann, Dieter .
APPLIED THERMAL ENGINEERING, 2010, 30 (11-12) :1326-1332
[10]   COMPUTATIONAL EXPERIENCE WITH DICOPT SOLVING MINLP PROBLEMS IN PROCESS SYSTEMS-ENGINEERING [J].
KOCIS, GR ;
GROSSMANN, IE .
COMPUTERS & CHEMICAL ENGINEERING, 1989, 13 (03) :307-315