May-Britt Hägg
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Research Subjects
Research Interests
May-Britt Hägg has a total of 15 co-authors. Here are the top co-authors by number of shared publications:
Arne Lindbråthen
Norwegian University of Science and Technology, Department of Chemical Engineering , Trondheim, Norway
4 shared publicationsJon Samseth
SINTEF Materials and Chemistry, Trondheim/Akershus University College, N-2001, Lillestrøm, N-7465, Norway
2 shared publicationsLei Shao
Department of Chemical Engineering, Faculty of Natural Sciences and Technology, Norwegian University of Science and Technology, Trondheim N-7491, Norway
2 shared publications- Xuezhong He
Department of Chemical Engineering, Guangdong Technion - Israel Institute of Technology, 241 Daxue Road, Shantou, Guangdong 515063, China
2 shared publications Arne Lindbrathen
Department of Chemical Engineering, Norwegian University of Science and Technology
1 shared publicationDavid Ryan Grainger
Norwegian University of Science and Technology, Department of Chemical Engineering , Trondheim, Norway
1 shared publication
Latest Publications
- 1 April 2019
- Vol. 5 (2) , 126-136
Techno-economic evaluation of helium recovery from natural gas; A comparison between inorganic and polymeric membrane technology
- 1 April 2019
- Vol. 5 (2) , 126-136
Techno-economic evaluation of helium recovery from natural gas; A comparison between inorganic and polymeric membrane technology
- 31 August 2016
- Published by Springer Nature
- p. 299-302
Carbon Membrane
- 31 August 2016
- Published by Springer Nature
- p. 804-807
Fossil Fuels Processing by Membrane Operations
- 31 August 2016
- Published by Springer Nature
- p. 1763-1765
Separation and Recovery of Gases, Multistage Process for
- 31 August 2016
- Published by Springer Nature
- p. 1763-1765
Separation and Recovery of Gases, Multistage Process for
- 31 August 2016
- Published by Springer Nature
- p. 849
Gas Permeation Unit (GPU)
- 31 August 2016
- Published by Springer Nature
- p. 850-852
Gas Permeation: Permeability, Permeance, and Separation Factor
- 31 August 2016
- Published by Springer Nature
- p. 850-852
Gas Permeation: Permeability, Permeance, and Separation Factor
- 12 December 2015
- Published by Springer Nature
- p. 1-4
Gas Permeation: Permeability, Permeance, and Separation Factor
- 12 December 2015
- Published by Springer Nature
- p. 1-4
Gas Permeation: Permeability, Permeance, and Separation Factor
- 27 August 2014
- Published by Wiley in AIChE Journal
- Vol. 60 (12) , 4174-4184
Hybrid FSC membrane for CO2 removal from natural gas: Experimental, process simulation, and economic feasibility analysis
The novel fixed‐site‐carrier (FSC) membranes were prepared by coating carbon nanotubes reinforced polyvinylamine/polyvinyl alcohol selective layer on top of ultrafiltration polysulfone support. Small pilot‐scale modules with membrane area of 110–330 cm2 were tested with high pressure permeation rig. The prepared hybrid FSC membranes show high CO2 permeance of 0.084–0.218 m3 (STP)/(m2 h bar) with CO2/CH4 selectivity of 17.9–34.7 at different feed pressures up to 40 bar for a 10% CO2 feed gas. Operating parameters of feed pressure, flow rate, and CO2 concentration were found to significantly influence membrane performance. HYSYS simulation integrated with ChemBrane and cost estimation was conducted to evaluate techno‐economic feasibility of a membrane process for natural gas (NG) sweetening. Simulation results indicated that the developed FSC membranes could be a promising candidate for CO2 removal from low CO2 concentration (10%) NGs with a low NG sweetening cost of 5.73E−3 $/Nm3 sweet NG produced. © 2014 American Institute of Chemical Engineers AIChE J 60: 4174–4184, 2014
- 27 August 2014
- Published by Wiley in AIChE Journal
- Vol. 60 (12) , 4174-4184
Hybrid FSC membrane for CO2 removal from natural gas: Experimental, process simulation, and economic feasibility analysis
The novel fixed‐site‐carrier (FSC) membranes were prepared by coating carbon nanotubes reinforced polyvinylamine/polyvinyl alcohol selective layer on top of ultrafiltration polysulfone support. Small pilot‐scale modules with membrane area of 110–330 cm2 were tested with high pressure permeation rig. The prepared hybrid FSC membranes show high CO2 permeance of 0.084–0.218 m3 (STP)/(m2 h bar) with CO2/CH4 selectivity of 17.9–34.7 at different feed pressures up to 40 bar for a 10% CO2 feed gas. Operating parameters of feed pressure, flow rate, and CO2 concentration were found to significantly influence membrane performance. HYSYS simulation integrated with ChemBrane and cost estimation was conducted to evaluate techno‐economic feasibility of a membrane process for natural gas (NG) sweetening. Simulation results indicated that the developed FSC membranes could be a promising candidate for CO2 removal from low CO2 concentration (10%) NGs with a low NG sweetening cost of 5.73E−3 $/Nm3 sweet NG produced. © 2014 American Institute of Chemical Engineers AIChE J 60: 4174–4184, 2014