Optimization of a flexible multi-generation system based on wood chip gasification and methanol production

• Published in: Applied energy 2017-04, Vol.192, p.337-359
• Main Authors: Lythcke-Jørgensen, Christoffer, Clausen, Lasse Røngaard, Algren, Loui, Hansen, Anders Bavnhøj, Münster, Marie, Gadsbøll, Rasmus Østergaard, Haglind, Fredrik
• Format: Article
• Language: English
• Subjects: Biomass gasification; Design optimization; Flexible multi-generation; Polygeneration; Process integration; Smart energy systems
• ISSN: 0306-2619; 1872-9118
• DOI: 10.1016/j.apenergy.2016.08.092

•A flexible multi-generation system (FMG) is modelled and optimized.•The FMG is based on an existing combined heat and power plant.•Retrofit options include a methanol-producing biorefinery and heat pumps.•The optimized design features a full-size biorefinery located next to industry.•Results stress that operation uncertainties must be considered when designing FMG. Flexible multi-generation systems (FMGs) consist of integrated and flexibly operated facilities that provide multiple links between the different sectors of the energy system. The present study treated the design optimization of a conceptual FMG which integrated a methanol-producing biorefinery with an existing combined heat and power (CHP) unit and industrial energy utility supply in the Danish city of Horsens. The objective was to optimize economic performance and minimize total CO2 emission of the FMG while it was required to meet the local district heating demand plus the thermal utility demand of the butchery. The design optimization considered: Selection, dimensioning, location and integration of processes; operation optimization with respect to both hourly variations in operating conditions over the year as well as expected long term energy system development; and uncertainty analysis considering both investment costs and operating conditions. Applying a previously developed FMG design methodology, scalable models of the considered processes were developed and the system design was optimized with respect to hourly operation over the period 2015–2035. The optimal design with respect to both economic and environmental performance involved a maximum-sized biorefinery located next to local industry rather than in connection with the existing CHP unit. As the local industry energy demands were limited when compared to the biorefinery dimensions considered, process integration synergies were found to be marginal when compared to the economic and environmental impact of the biorefinery for the present case. Assessing the impact of uncertainties on the estimated FMG performances, the net present value (NPV) of the optimal design was estimated to vary within the range 252.5–1471.6M€ in response to changes of ±25% in investment costs and methanol price, and considering two different electricity price scenarios. In addition, a change in the interest rate from 5% to 20% was found to reduce the lower bound of the NPV to 181.3M€ for reference operating conditions. The results suggest that the applied