Pilot-scale CO2 capture demonstration of stripper interheating using 30 wt% MEA at a Waste-to-Energy facility

被引:0
|
作者
Vinjarapu, Sai Hema Bhavya [1 ]
Neerup, Randi [1 ]
Larsen, Anders Hellerup [1 ]
Villadsen, Sebastian Nis Bay [1 ]
Jensen, Soren [2 ]
Karlsson, Jakob Lindkvist [2 ]
Kappel, Jannik [3 ]
Lassen, Henrik [3 ]
Blinksbjerg, Peter [3 ]
von Solms, Nicolas [1 ]
Fosbol, Philip Loldrup [1 ]
机构
[1] Tech Univ Denmark DTU, Ctr Energy Resources Engn CERE, Dept Chem Engn, Soltofts Plads,Bldg 229, DK-2800 Lyngby, Denmark
[2] Pentair Union Engn AS, Snaremosevej 27, DK-7000 Fredericia, Denmark
[3] ARC, Amager Bakke, Vindmollevej 6, DK-2300 Copenhagen, Denmark
关键词
Climate action; Stripper interheating; Heat integration; Pilot scale demonstration; Process optimisation; TECHNOECONOMIC ASSESSMENT; AQUEOUS MONOETHANOLAMINE; POWER-PLANTS; FLUE-GAS; TECHNOLOGY; CONFIGURATIONS; PERFORMANCE; AMINE; INTEGRATION;
D O I
10.1016/j.energy.2025.134973
中图分类号
O414.1 [热力学];
学科分类号
摘要
Post-combustion CO2 capture is a widely recognised technology for controlling industrial CO2 emissions. However, issues like the substantial energy demands for solvent regeneration still need to be solved. The current work aims to discuss the outcomes of process optimisation within a pilot-scale CO2 capture facility by implementing interheating in the stripper to reduce energy consumption. The pilot-scale experiments were executed at Amager Bakke, a Waste-to-Energy plant in Copenhagen, Denmark. These tests used 30 wt% Monoethanolamine as the solvent. A semi-lean solvent from the middle of the stripper is withdrawn for external heating by an interheater and fed to the stripper at the same height. A steam generator with adjustable electrical duty is used as the heat source for the interheater. The novelty of this work lies in the pilot scale demonstration of stripper interheating at an industrial facility, which has seldom been done. The objective is to experimentally demonstrate the performance of the Interheating configuration at the pilot scale and analyse the potential improvements in the energy consumption of the process. The interheating experiments were conducted by varying the reboiler duty in the range of 12 to 20 kW and the interheater duty in the range of 2 to 5 kW while maintaining a solvent flow of 267 kg/h and a flue gas flow of 99 kg/h. The results provide several possible scenarios, are discussed in detail, and are compared to previously obtained base case results. While maintaining a capture efficiency of around 83%, stripper interheating has demonstrated a specific reboiler duty of 2.71 GJ/tonne CO2 compared to 3.71 GJ/tonne CO2 achieved by the base case operation. A 3% reduction in the specific reboiler duty was achieved by interheating at a capture efficiency slightly over 90%. A preliminary model based on the experimental results has shown a further reduction of SRD to 2.25 GJ/tonne CO2 at high capture efficiencies.
引用
收藏
页数:25
相关论文
共 50 条
  • [1] Pilot-scale CO2 capture demonstration of heat integration through split flow configuration using 30 wt % MEA at a Waste-to-Energy facility
    Vinjarapu, Sai Hema Bhavya
    Neerup, Randi
    Larsen, Anders Hellerup
    Villadsen, Sebastian Nis Bay
    von Solms, Nicolas
    Jensen, Soren
    Karlsson, Jakob Lindkvist
    Kappel, Jannik
    Lassen, Henrik
    Blinksbjerg, Peter
    Fosbol, Philip Loldrup
    SEPARATION AND PURIFICATION TECHNOLOGY, 2024, 345
  • [2] Results from pilot-scale CO2 capture testing using 30 wt% MEA at a Waste-to-Energy facility: Optimisation through parametric analysis
    Vinjarapu, Sai Hema Bhavya
    Neerup, Randi
    Larsen, Anders Hellerup
    Jorsboe, Jens Kristian
    Villadsen, Sebastian Nis Bay
    Jensen, Soren
    Karlsson, Jakob Lindkvist
    Kappel, Jannik
    Lassen, Henrik
    Blinksbjerg, Peter
    von Solms, Nicolas
    Fosbol, Philip Loldrup
    APPLIED ENERGY, 2024, 355
  • [3] Mobile pilot plant for CO2 capture in biogas upgrading using 30 wt% MEA
    Jorsboe, Jens Kristian
    Vinjarapu, Sai Hema Bhavya
    Neerup, Randi
    Moller, Andreas Christian
    Jensen, Soren
    Abildskov, Jens
    Fosbol, Philip
    FUEL, 2023, 350
  • [4] NORWEGIANS CAPTURE CO2 FROM WASTE-TO-ENERGY
    Scott, Alex
    CHEMICAL & ENGINEERING NEWS, 2016, 94 (05) : 18 - 18
  • [5] PILOT-SCALE POSTCOMBUSTION CO2 CAPTURE USING ACTIVATED CARBON
    Smutna, J.
    Stefanica, J.
    Hajek, P.
    Ciahotny, K.
    Machac, P.
    PROCEEDINGS OF THE 3RD INTERNATIONAL CONFERENCE ON CHEMICAL TECHNOLOGY, 2015, : 71 - 74
  • [6] Dynamic simulation and analysis of a pilot-scale CO2 post-combustion capture unit using piperazine and MEA
    Gaspar, Jozsef
    Ricardez-Sandoval, Luis
    Jorgensen, John Bagterp
    Foshol, Philip Loldrup
    IFAC PAPERSONLINE, 2016, 49 (07): : 645 - 650
  • [7] Solvent degradation and emissions from a CO2 capture pilot at a waste-to-energy plant
    Neerup, Randi
    Rasmussen, Valdemar E.
    Vinjarapu, Sai H. B.
    Larsen, Anders H.
    Shi, Meng
    Andersen, Christina
    Fuglsang, Karsten
    Gram, Lars K.
    Nedenskov, Jonas
    Kappel, Jannik
    Blinksbjerg, Peter
    Jensen, Soren
    Karlsson, Jakob L.
    Borgquist, Sebastian
    Jorsboe, Jens K.
    Villadsen, Sebastian N. B.
    Fosbol, Philip L.
    JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING, 2023, 11 (06):
  • [8] A Controllability Analysis of a Pilot-Scale CO2 Capture Plant Using Ionic Liquids
    Valencia-Marquez, Darinel
    Flores-Tlacuahuac, Antonio
    Ricardez-Sandoval, Luis
    AICHE JOURNAL, 2016, 62 (09) : 3298 - 3309
  • [9] Pilot-scale evaluations of advanced solvents for postcombustion CO2 capture
    Kay, John P.
    Jensen, Melanie D.
    Fiala, Nathan J.
    12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12, 2014, 63 : 1903 - 1910
  • [10] Pilot plant studies of the CO2 capture performance of aqueous MEA and mixed MEA/MDEA solvents at the University of Regina CO2 capture technology development plant and the Boundary Dam CO2 capture demonstration
    Idem, R
    Wilson, M
    Tontiwachwuthikul, P
    Chakma, A
    Veawab, A
    Aroonwilas, A
    Gelowitz, D
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (08) : 2414 - 2420