- Email: [email protected]
Results from 30 wt% MEA Performance Testing at the CO2 Technology Centre Mongstad
Available online at www.sciencedirect.com
ScienceDirect Energy Procedia 114 (2017) 1146 – 1157
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Gassnova SF, Dokkvegen 10, 3920 Porsgrunn, Norway b Statoil ASA, PO Box 8500, 4035 Stavanger, Norway c Sasol Technology, PO Box 5486, Johannesburg 2000, South Africa d Shell Global Solutions International B.V., PO Box 663, 2501CR The Hague, The Netherlands e CO2 Technology Centre Mongstad (TCM DA), 5954 Mongstad, Norway
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© 2017 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license 7KH$XWKRUV3XEOLVKHGE\(OVHYLHU/WG (http://creativecommons.org/licenses/by-nc-nd/4.0/). 3HHUUHYLHZXQGHUUHVSRQVLELOLW\RIWKHRUJDQL]LQJFRPPLWWHHRI*+*7 Peer-review under responsibility of the organizing committee of GHGT-13.
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1876-6102 © 2017 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/). Peer-review under responsibility of the organizing committee of GHGT-13. doi:10.1016/j.egypro.2017.03.1276
Erik Gjernes et al. / Energy Procedia 114 (2017) 1146 – 1157
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Method:B1
92 90 88 86 20ͲJul
19ͲJul
18ͲJul
17ͲJul
16ͲJul
15ͲJul
14ͲJul
84 13ͲJul
CO2 massbalanceclosure[%]
104
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Erik Gjernes et al. / Energy Procedia 114 (2017) 1146 – 1157
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20,000
0.20
20000
0.15
10,000
0.15
10000
0.10
0
0.10
0 03ͲSep
30000
0.20
02ͲSep
0.25
01ͲSep
30,000
31ͲAug
40000
0.25
30ͲAug
0.30
29ͲAug
40,000
28ͲAug
50000
0.30
27ͲAug
0.35
26ͲAug
50,000
Loading[mole/mole]
60000
0.35
Leanamineflow[kg/h]
0.40
25ͲAug
60,000
24ͲAug
70000
0.40
23ͲAug
0.45
22ͲAug
70,000
21ͲAug
80000
0.45
20ͲAug
0.50
Leanamineflow[kg/h]
123C 121C
122C
121C
120C
118C 119C
118C
116.5C
118C 118C 117.5C
119C
120C
121C
120C
118C
80,000
19ͲAug
90000
0.50
18ͲAug
100000
0.55
17ͲAug
0.60
90,000
16ͲAug
100,000
0.55
15ͲAug
0.60
14ͲAug
Loading[mole/mole]
117C
116C
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Erik Gjernes et al. / Energy Procedia 114 (2017) 1146 – 1157
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60°C,0mbarg
14/08/2015
26/08/2015
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4.5
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4.0
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ScienceDirect Energy Procedia 114 (2017) 1146 – 1157
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Gassnova SF, Dokkvegen 10, 3920 Porsgrunn, Norway b Statoil ASA, PO Box 8500, 4035 Stavanger, Norway c Sasol Technology, PO Box 5486, Johannesburg 2000, South Africa d Shell Global Solutions International B.V., PO Box 663, 2501CR The Hague, The Netherlands e CO2 Technology Centre Mongstad (TCM DA), 5954 Mongstad, Norway
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© 2017 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license 7KH$XWKRUV3XEOLVKHGE\(OVHYLHU/WG (http://creativecommons.org/licenses/by-nc-nd/4.0/). 3HHUUHYLHZXQGHUUHVSRQVLELOLW\RIWKHRUJDQL]LQJFRPPLWWHHRI*+*7 Peer-review under responsibility of the organizing committee of GHGT-13.
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1876-6102 © 2017 The Authors. Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/). Peer-review under responsibility of the organizing committee of GHGT-13. doi:10.1016/j.egypro.2017.03.1276
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7
8
9
CO2 inletconsentration(%wet)
10
0.60
122.5
0.50
122.0
0.40
121.5
0.30
121.0
0.20
120.5 120.0
0.10 0
1
2
3
4
5
6
7
8
9
10
Stripperbottomtemp.[°C]
140,000
Loading[mole/mole]
4.0
Leansolventflow[kg/h]
SRD[MJ/kgCO2]
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CO2 inletconsentration(%wet)
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Erik Gjernes et al. / Energy Procedia 114 (2017) 1146 – 1157
1157
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