Operational Experience and Initial Results from the First Test Period at CO2 Technology Centre Mongstad

Andersson, Vibeke; Wittmeyer, Kristina; Gorset, Oddvar; Maree, Yolandi; Sanden, Knut

doi:10.1016/j.egypro.2013.06.564

Cited by 8 publications

(13 citation statements)

References 1 publication

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“…The Technology Centre Mongstad (TCM) test facility is located next to the Equinor oil renery in Mongstad, Norway. The TCM amine absorption plant is designed to be exible with two possible congurations that typically captures 85% of the CO 2 from dierent ue gas slipstreams [38,39].…”

Section: Plant Descriptionmentioning

confidence: 99%

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Demonstrating flexible operation of the Technology Centre Mongstad (TCM) CO2 capture plant

Bui

Flø

Cazenove

et al. 2020

International Journal of Greenhouse Gas Control

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Section: Plant Descriptionmentioning

confidence: 99%

“…A detailed description of the measurement instruments used to monitor stream conditions and composition is available in previous contributions [38,44,39,41,45], which also include a detailed analysis of measurement accuracy, bias and precision (i.e., quantication of uncertainty and error).…”

Section: Experimental Measurements and Data Processingmentioning

confidence: 99%

Demonstrating flexible operation of the Technology Centre Mongstad (TCM) CO2 capture plant

Bui

Flø

Cazenove

et al. 2020

International Journal of Greenhouse Gas Control

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“…Post combustion CO2 capture using absorption processes is currently the most mature technology for CCS and over the last years several pilot plants and test centres have been or are being built to test a variety of absorbents, e.g. Technology Centre Mongstad (TCM) in Norway (Andersson et al, 2013;Jönsson and Telikapalli, 2013), International test Centre (ITC) in Canada (Skoropad et al, 2003;Wilson et al, 2003), several pilots in Australia (CSIRO) (Cousins et al, 2012). Additionally a full scale plant has been built at Boundary Dam Canada.…”

Section: Introductionmentioning

confidence: 99%

Influence of experimental setup on amine degradation

Vevelstad

Grimstvedt

Knuutila

et al. 2014

International Journal of Greenhouse Gas Control

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“…solvent flow rates, absorber packing heights, stripper pressures, reboiler heat duties, lean amine and cross heat exchanger duties, absorber water wash temperatures and flow rates with or without acid injections, anti-foam solution injections, etc. [1,2] The campaign described in the current paper was conducted at TCM DA in the period December 2013 to February 2014 as a part of Aker Solutions' test period. In general, during the campaign the aqueous 30 wt% monoethanolamine (MEA) solvent system was applied treating the flue gas from the CHP plant.…”

Section: Introductionmentioning

confidence: 99%

Results of Amine Plant Operations from 30 wt% and 40 wt% Aqueous MEA Testing at the CO2 Technology Centre Mongstad

Brigman

Shah²,

Falk-Pedersen³

et al. 2014

Energy Procedia

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An amine plant campaign has been performed at the CO 2 Technology Centre Mongstad applying the aqueous 30 wt% and 40 wt% monoethanolamine (MEA) solvent systems for treatment of flue gas from a combined heat and power (CHP) plant. CHP flue gas flow rates were ranging from about 40.000 Sm 3 /h to 60.000 Sm 3 /h and the CO 2 content was about 3.5 vol%.Minimum specific reboiler duties (SRD) of respectively 4.0 MJ/kg CO 2 and 3.7 MJ/kg CO 2 were obtained for the aqueous 30 wt% MEA solvent system without and with the addition of anti-foam solution. A minimum SRD of 3.4 MJ/kg CO 2 was obtained for the aqueous 40 wt% MEA solvent system. Lower SRD and absorber liquid to gas (L/G) ratios were obtained with higher concentration MEA solvents.Increased absorber packing heights resulted in lower SRD. Variation in flue gas supply flow rates and corresponding variations in solvent flow rates, i.e. constant L/G ratios, did not yield any significant variations in SRD. Decreased flue gas supply temperatures resulted in lower SRD.For any future large scale post-combustion capture (PCC) amine plant, engineering aspects such as the flue gas supply temperature and instrumentation monitoring CO 2 content in the flue gas must be evaluated to avoid the chemical equilibrium pinch behavior. Engineering and environmental aspects related to the use of anti-foam solutions for future large scale PCC amine plants must also be considered.

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Operational Experience and Initial Results from the First Test Period at CO2 Technology Centre Mongstad

Cited by 8 publications

References 1 publication

Demonstrating flexible operation of the Technology Centre Mongstad (TCM) CO2 capture plant

Demonstrating flexible operation of the Technology Centre Mongstad (TCM) CO2 capture plant

Influence of experimental setup on amine degradation

Results of Amine Plant Operations from 30 wt% and 40 wt% Aqueous MEA Testing at the CO2 Technology Centre Mongstad

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