Randi Neerup

Technical University of Denmark

Denmark

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Articles (25)

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2025

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2022

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2022

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2022

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2022

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2021

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2021

Collaborators (11)

Kaj Thomsen

Technical University of Denmark

DENMARK

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Brian Elmegaard

Technical University of Denmark

DENMARK

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Jonas Kjær Jensen

Technical University of Denmark

DENMARK

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Rikke Cilius Pedersen

Technical University of Denmark

DENMARK

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Philip Loldrup Fosbøl

Technical University of Denmark

DENMARK

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Sai Hema Bhavya Vinjarapu

Technical University of Denmark

DENMARK

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Sebastian Borgquist

Technical University of Denmark

DENMARK

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Lucas Corrêa

Technical University of Denmark

DENMARK

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Rolf W. Berg

Technical University of Denmark

DENMARK

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Jens Abildskov

Technical University of Denmark

DENMARK

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Can Demir

Technical University of Denmark

DENMARK

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Randi Neerup

Research Interests

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Articles (25)

Pilot-scale CO2 capture in a cement plant with CESAR1: Higher stripper pressure reduces energy demand and compression work but increases solvent degradation

Pilot-scale CO2 capture in a cement plant with CESAR1: Comparative analysis of specific reboiler duty across advanced process configurations

The cost of impurities: A techno-economic assessment on conditioning of captured CO2 to commercial specifications

CO2 capture pilot campaign: Understanding solvent degradation of CESAR1 in cement plant operations

Density data for further understanding of CO2 capture using piperazine solvents

Pilot-Scale CO2 capture in a cement plant with CESAR1

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

Power-to-X gas desulfurization technology: Demonstration and parameter analysis

Thermodynamic modelling of the solubility in piperazine (PZ) promoted aqueous solutions of methyldiethanolamine (MDEA) using the extended UNIQUAC

Learnings from up-scaling CO2 capture: Challenges and experiences with pilot work

Pilot-scale CO2 capture demonstration of heat integration through split flow configuration using 30 wt% MEA at a Waste-to-Energy facility

Heat of absorption of CO2 in 30 wt% MEA with monoethyleneglycol and urea as vapour reduction additives

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

Demonstration of water-lean 30 wt% MEA + 15 wt% MEG with rich solvent recycle for biogas upgrading

Experimental solubility of FeCO3 in aqueous 3-20 wt% KCl at 25-80°C

Solubility of FeCO3 in aqueous NaCl, and aqueous HCl

FeCO3 Synthesis Pathways: The Influence of Temperature, Duration, and Pressure

Measurements and modelling of FeCO3 solubility in water relevant to corrosion and CO2 mineralization

Mobile pilot plant for CO2 capture in biogas upgrading using 30 wt% MEA

Review of barium sulphate solubility measurements

A Call for Standards in the CO2 Value Chain

Influence of CO2 on the Solubility of Potassium Glycinate in Glycine–KOH–H2O, Glycine–KHCO3–H2O, and Glycine–KOH–KHCO3–H2O

Solid–Liquid Phase Boundaries in the System: Glycine–NaOH–NaHCO3–H2O

Solid–Liquid Equilibria of a 30 wt % Aqueous Monoethanolamine Solution Containing Urea and Monoethylene Glycol

Solubility of NaHCO3 in Systems of Aqueous Glycols (Monoethylene Glycol, Diethylene Glycol, Triethylene Glycol, and Tetraethylene Glycol): The Role of Solvation

Collaborators (11)

Kaj Thomsen

Brian Elmegaard

Jonas Kjær Jensen

Rikke Cilius Pedersen

Philip Loldrup Fosbøl

Sai Hema Bhavya Vinjarapu

Sebastian Borgquist

Lucas Corrêa

Rolf W. Berg

Jens Abildskov

Can Demir

Make your next move.

Demonstration of water-lean 30 wt% MEA + 15 wt% MEG with rich solvent recycle for biogas upgrading