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

Authors :
Vinjarapu, Sai Hema Bhavya
Neerup, Randi
Larsen, Anders Hellerup
Jørsboe, Jens Kristian
Villadsen, Sebastian Nis Bay
Jensen, Søren
Karlsson, Jakob Lindkvist
Kappel, Jannik
Lassen, Henrik
Blinksbjerg, Peter
von Solms, Nicolas
Fosbøl, Philip Loldrup
Vinjarapu, Sai Hema Bhavya
Neerup, Randi
Larsen, Anders Hellerup
Jørsboe, Jens Kristian
Villadsen, Sebastian Nis Bay
Jensen, Søren
Karlsson, Jakob Lindkvist
Kappel, Jannik
Lassen, Henrik
Blinksbjerg, Peter
von Solms, Nicolas
Fosbøl, Philip Loldrup
Source :
Vinjarapu , S H B , Neerup , R , Larsen , A H , Jørsboe , J K , Villadsen , S N B , Jensen , S , Karlsson , J L , Kappel , J , Lassen , H , Blinksbjerg , P , von Solms , N & Fosbøl , P L 2024 , ' Results from pilot-scale CO 2 capture testing using 30 wt% MEA at a Waste-to-Energy facility: Optimisation through parametric analysis ' , Applied Energy , vol. 355 , 122193 .
Publication Year :
2024

Abstract

Post-combustion carbon capture is a well-established technology for removing CO 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 CO/day) studies of CO 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 CO 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.

Details

Database :
OAIster
Journal :
Vinjarapu , S H B , Neerup , R , Larsen , A H , Jørsboe , J K , Villadsen , S N B , Jensen , S , Karlsson , J L , Kappel , J , Lassen , H , Blinksbjerg , P , von Solms , N & Fosbøl , P L 2024 , ' Results from pilot-scale CO 2 capture testing using 30 wt% MEA at a Waste-to-Energy facility: Optimisation through parametric analysis ' , Applied Energy , vol. 355 , 122193 .
Notes :
application/pdf, English
Publication Type :
Electronic Resource
Accession number :
edsoai.on1426750113
Document Type :
Electronic Resource