Results from pilot-scale CO2 capture testing using 30 wt% MEA at a Waste-to-Energy facility: Optimisation through parametric analysis

被引:14
|
作者
Vinjarapu, Sai Hema Bhavya [1 ]
Neerup, Randi [1 ]
Larsen, Anders Hellerup [1 ]
Jorsboe, Jens Kristian [1 ]
Villadsen, Sebastian Nis Bay
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, Bldg 229, DK-2800 Kongens Lyngby, Denmark
[2] Pentair Union Engn A S, Snaremosevej 27, DK-7000 Fredericia, Denmark
[3] Amager Bakke ARC, Vindmollevej 6, DK-2300 Copenhagen, Denmark
关键词
CO2; capture; Waste-to-Energy; Specific reboiler duty (SRD); Capture efficiency; Stripping intensity; TECHNOLOGY CENTER MONGSTAD; AMINE-BASED SOLVENTS; FLUE-GAS; CARBON CAPTURE; REACTIVE ABSORPTION; POWER-PLANT; EXPERIMENTAL VALIDATION; PERFORMANCE; STORAGE; MODEL;
D O I
10.1016/j.apenergy.2023.122193
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Post-combustion carbon capture is a well-established technology for removing CO2 from industrial emissions. However, research is still underway to optimise the process and make it more energy efficient. The current work aims to present the results from pilot-scale (with a capacity of 1 tonne CO2/day) studies of CO2 capture conducted at Amager Bakke, a Waste-to-Energy facility in Copenhagen, Denmark. The pilot operation is fully automated, and the process control structure helps achieve multiple steady states at regular intervals. In addition, the pilot is capable of several configurations which can assist in optimising the energy required for solvent regeneration. The current work discusses the base case configuration of the pilot plant by employing 30 wt% MEA as the solvent. Experiments were conducted to analyse the influence of reboiler duty, solvent flow rate, and gas flow rate on the pilot's performance. The influence of these parameters on several aspects is discussed in detail, and recommendations for the optimal operation of such plants are provided. An optimum specific reboiler duty of 3.46 GJ/tonne CO2 is obtained at a solvent flow rate of 306 kg/h, flue gas flow rate of 113 kg/h, and reboiler duty of 17.5 kW excluding heat loss.
引用
收藏
页数:41
相关论文
共 50 条
  • [1] Pilot-scale CO2 capture demonstration of stripper interheating using 30 wt% MEA at a Waste-to-Energy facility
    Vinjarapu, Sai Hema Bhavya
    Neerup, Randi
    Larsen, Anders Hellerup
    Villadsen, Sebastian Nis Bay
    Jensen, Soren
    Karlsson, Jakob Lindkvist
    Kappel, Jannik
    Lassen, Henrik
    Blinksbjerg, Peter
    von Solms, Nicolas
    Fosbol, Philip Loldrup
    ENERGY, 2025, 320
  • [2] 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
  • [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] 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
  • [6] 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):
  • [7] 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
  • [8] 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
  • [9] Parametric testing of a pilot-scale design for a moving-bed CO2 capture system using low-temperature steam
    Okumura, Takeshi
    Yoshizawa, Katsuhiro
    Nishibe, Shohei
    Iwasaki, Hidekazu
    Kazari, Masahide
    Hori, Toru
    13TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-13, 2017, 114 : 2322 - 2329
  • [10] Results from 30 wt% MEA Performance Testing at the CO 2 Technology Centre Mongstad
    Gjernes, Erik
    Pedersen, Steinar
    Cents, Toine
    Watson, Guillaume
    Fostas, Berit F.
    Shah, Muhammad Ismail
    Lombardo, Gerard
    Desvignes, Coralie
    Flo, Nina Enaasen
    Morken, Anne Kolstad
    de Cazenove, Thomas
    Faramarzi, Leila
    Hamborg, Espen Steinseth
    13TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-13, 2017, 114 : 1146 - 1157